EP3387024B1 - Monofunctional or telechelic copolymer of 1,3-diene and ethylene or alpha-monoolefin - Google Patents
Monofunctional or telechelic copolymer of 1,3-diene and ethylene or alpha-monoolefin Download PDFInfo
- Publication number
- EP3387024B1 EP3387024B1 EP16809754.1A EP16809754A EP3387024B1 EP 3387024 B1 EP3387024 B1 EP 3387024B1 EP 16809754 A EP16809754 A EP 16809754A EP 3387024 B1 EP3387024 B1 EP 3387024B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- copolymer
- sime
- group
- function
- formula
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 229920001577 copolymer Polymers 0.000 title claims description 127
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 title claims description 30
- 239000005977 Ethylene Substances 0.000 title claims description 28
- LLVWLCAZSOLOTF-UHFFFAOYSA-N 1-methyl-4-[1,4,4-tris(4-methylphenyl)buta-1,3-dienyl]benzene Chemical compound C1=CC(C)=CC=C1C(C=1C=CC(C)=CC=1)=CC=C(C=1C=CC(C)=CC=1)C1=CC=C(C)C=C1 LLVWLCAZSOLOTF-UHFFFAOYSA-N 0.000 title 1
- 239000000178 monomer Substances 0.000 claims description 51
- 239000000203 mixture Substances 0.000 claims description 45
- 239000000460 chlorine Substances 0.000 claims description 32
- 238000000034 method Methods 0.000 claims description 31
- 238000006243 chemical reaction Methods 0.000 claims description 23
- 239000003795 chemical substances by application Substances 0.000 claims description 23
- QGZKDVFQNNGYKY-UHFFFAOYSA-O ammonium group Chemical group [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 21
- 150000001875 compounds Chemical class 0.000 claims description 17
- 150000001993 dienes Chemical class 0.000 claims description 16
- 238000012546 transfer Methods 0.000 claims description 16
- 125000003983 fluorenyl group Chemical group C1(=CC=CC=2C3=CC=CC=C3CC12)* 0.000 claims description 12
- 238000002360 preparation method Methods 0.000 claims description 12
- 229920001971 elastomer Polymers 0.000 claims description 11
- 125000000058 cyclopentadienyl group Chemical group C1(=CC=CC1)* 0.000 claims description 10
- 229910052799 carbon Inorganic materials 0.000 claims description 9
- 239000012968 metallocene catalyst Substances 0.000 claims description 9
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 8
- 125000004432 carbon atom Chemical group C* 0.000 claims description 8
- 229910052757 nitrogen Inorganic materials 0.000 claims description 8
- 229910052761 rare earth metal Inorganic materials 0.000 claims description 8
- 229910052725 zinc Inorganic materials 0.000 claims description 8
- 239000011701 zinc Substances 0.000 claims description 8
- 229910052782 aluminium Inorganic materials 0.000 claims description 7
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical group [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 7
- 125000003454 indenyl group Chemical group C1(C=CC2=CC=CC=C12)* 0.000 claims description 7
- 150000002602 lanthanoids Chemical group 0.000 claims description 7
- 150000002910 rare earth metals Chemical group 0.000 claims description 7
- 125000004429 atom Chemical group 0.000 claims description 6
- 125000002147 dimethylamino group Chemical group [H]C([H])([H])N(*)C([H])([H])[H] 0.000 claims description 6
- 238000003780 insertion Methods 0.000 claims description 6
- 230000037431 insertion Effects 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 229910052751 metal Inorganic materials 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 6
- 230000003197 catalytic effect Effects 0.000 claims description 5
- 238000007334 copolymerization reaction Methods 0.000 claims description 5
- 229910052710 silicon Inorganic materials 0.000 claims description 5
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 4
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 4
- 239000004411 aluminium Substances 0.000 claims description 4
- 150000001412 amines Chemical class 0.000 claims description 4
- 239000000806 elastomer Substances 0.000 claims description 4
- 229910052736 halogen Inorganic materials 0.000 claims description 4
- 150000002367 halogens Chemical class 0.000 claims description 4
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 claims description 3
- 229910052779 Neodymium Inorganic materials 0.000 claims description 3
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 3
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 3
- 229910052801 chlorine Inorganic materials 0.000 claims description 3
- 150000002576 ketones Chemical class 0.000 claims description 3
- QEFYFXOXNSNQGX-UHFFFAOYSA-N neodymium atom Chemical group [Nd] QEFYFXOXNSNQGX-UHFFFAOYSA-N 0.000 claims description 3
- 150000003141 primary amines Chemical class 0.000 claims description 3
- 239000010703 silicon Substances 0.000 claims description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 claims description 2
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims description 2
- 229910052794 bromium Inorganic materials 0.000 claims description 2
- 239000011737 fluorine Substances 0.000 claims description 2
- 229910052731 fluorine Inorganic materials 0.000 claims description 2
- 229910052740 iodine Inorganic materials 0.000 claims description 2
- 239000011630 iodine Substances 0.000 claims description 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 57
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 49
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 36
- 229920000642 polymer Polymers 0.000 description 32
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 24
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- -1 aromatic alcohols Chemical class 0.000 description 15
- 125000000325 methylidene group Chemical group [H]C([H])=* 0.000 description 15
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 14
- 230000015572 biosynthetic process Effects 0.000 description 14
- 238000006116 polymerization reaction Methods 0.000 description 14
- 238000003786 synthesis reaction Methods 0.000 description 14
- 238000000425 proton nuclear magnetic resonance spectrum Methods 0.000 description 12
- 239000002904 solvent Substances 0.000 description 12
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 10
- 239000011777 magnesium Substances 0.000 description 10
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 9
- 230000004048 modification Effects 0.000 description 9
- 238000012986 modification Methods 0.000 description 9
- 229950011008 tetrachloroethylene Drugs 0.000 description 9
- 125000001931 aliphatic group Chemical group 0.000 description 6
- 125000003277 amino group Chemical group 0.000 description 6
- 150000001721 carbon Chemical group 0.000 description 6
- 229910052747 lanthanoid Inorganic materials 0.000 description 6
- 238000005481 NMR spectroscopy Methods 0.000 description 5
- 238000004458 analytical method Methods 0.000 description 5
- 229910052786 argon Inorganic materials 0.000 description 5
- 238000010511 deprotection reaction Methods 0.000 description 5
- 238000006460 hydrolysis reaction Methods 0.000 description 5
- 150000005673 monoalkenes Chemical class 0.000 description 5
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 4
- DURPTKYDGMDSBL-UHFFFAOYSA-N 1-butoxybutane Chemical compound CCCCOCCCC DURPTKYDGMDSBL-UHFFFAOYSA-N 0.000 description 4
- GQEZCXVZFLOKMC-UHFFFAOYSA-N 1-hexadecene Chemical compound CCCCCCCCCCCCCCC=C GQEZCXVZFLOKMC-UHFFFAOYSA-N 0.000 description 4
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 4
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 4
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 4
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 4
- 239000012300 argon atmosphere Substances 0.000 description 4
- UHOVQNZJYSORNB-MZWXYZOWSA-N benzene-d6 Chemical compound [2H]C1=C([2H])C([2H])=C([2H])C([2H])=C1[2H] UHOVQNZJYSORNB-MZWXYZOWSA-N 0.000 description 4
- 230000008034 disappearance Effects 0.000 description 4
- 229910052744 lithium Inorganic materials 0.000 description 4
- 229910052700 potassium Inorganic materials 0.000 description 4
- 239000011591 potassium Substances 0.000 description 4
- 239000012429 reaction media Substances 0.000 description 4
- 239000000523 sample Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- PBKONEOXTCPAFI-UHFFFAOYSA-N 1,2,4-trichlorobenzene Chemical compound ClC1=CC=C(Cl)C(Cl)=C1 PBKONEOXTCPAFI-UHFFFAOYSA-N 0.000 description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000002378 acidificating effect Effects 0.000 description 3
- 229910052783 alkali metal Inorganic materials 0.000 description 3
- 150000001340 alkali metals Chemical class 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000007306 functionalization reaction Methods 0.000 description 3
- 239000008246 gaseous mixture Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 238000001542 size-exclusion chromatography Methods 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- UHPDDKDFATYPJX-UHFFFAOYSA-N 2,2,5,5-tetramethyl-1-propyl-1,2,5-azadisilolidine Chemical group CCCN1[Si](C)(C)CC[Si]1(C)C UHPDDKDFATYPJX-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- 239000003963 antioxidant agent Substances 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- 125000004122 cyclic group Chemical group 0.000 description 2
- ZSWFCLXCOIISFI-UHFFFAOYSA-N endo-cyclopentadiene Natural products C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical compound II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 description 2
- 239000003446 ligand Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 2
- 150000002902 organometallic compounds Chemical class 0.000 description 2
- 150000003335 secondary amines Chemical class 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- BKBUBAVZGMRPAK-UHFFFAOYSA-N 1-(3-bromopropyl)-2,2,5,5-tetramethyl-1,2,5-azadisilolidine Chemical compound C[Si]1(C)CC[Si](C)(C)N1CCCBr BKBUBAVZGMRPAK-UHFFFAOYSA-N 0.000 description 1
- 238000005160 1H NMR spectroscopy Methods 0.000 description 1
- XMSZMOKNRMTSCQ-UHFFFAOYSA-N BrCCCN1[Si](CC[Si]1(C)C)(C)C.[Mg] Chemical compound BrCCCN1[Si](CC[Si]1(C)C)(C)C.[Mg] XMSZMOKNRMTSCQ-UHFFFAOYSA-N 0.000 description 1
- NLZUEZXRPGMBCV-UHFFFAOYSA-N Butylhydroxytoluene Chemical compound CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 NLZUEZXRPGMBCV-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- OKTJSMMVPCPJKN-OUBTZVSYSA-N Carbon-13 Chemical compound [13C] OKTJSMMVPCPJKN-OUBTZVSYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 241001080024 Telles Species 0.000 description 1
- 125000004036 acetal group Chemical group 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- 238000000149 argon plasma sintering Methods 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- 150000005840 aryl radicals Chemical class 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 239000000539 dimer Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004210 ether based solvent Substances 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 125000005842 heteroatom Chemical group 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 125000002346 iodo group Chemical group I* 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002530 phenolic antioxidant Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000005956 quaternization reaction Methods 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 239000012763 reinforcing filler Substances 0.000 description 1
- 239000012488 sample solution Substances 0.000 description 1
- 229910052706 scandium Inorganic materials 0.000 description 1
- SIXSYDAISGFNSX-UHFFFAOYSA-N scandium atom Chemical compound [Sc] SIXSYDAISGFNSX-UHFFFAOYSA-N 0.000 description 1
- 239000011265 semifinished product Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- 150000003512 tertiary amines Chemical class 0.000 description 1
- CZDYPVPMEAXLPK-UHFFFAOYSA-N tetramethylsilane Chemical compound C[Si](C)(C)C CZDYPVPMEAXLPK-UHFFFAOYSA-N 0.000 description 1
- 125000000026 trimethylsilyl group Chemical group [H]C([H])([H])[Si]([*])(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910052727 yttrium Inorganic materials 0.000 description 1
- VWQVUPCCIRVNHF-UHFFFAOYSA-N yttrium atom Chemical compound [Y] VWQVUPCCIRVNHF-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/02—Ethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/12—Hydrolysis
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/18—Introducing halogen atoms or halogen-containing groups
- C08F8/20—Halogenation
- C08F8/22—Halogenation by reaction with free halogens
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2410/00—Features related to the catalyst preparation, the catalyst use or to the deactivation of the catalyst
- C08F2410/01—Additive used together with the catalyst, excluding compounds containing Al or B
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2810/00—Chemical modification of a polymer
- C08F2810/40—Chemical modification of a polymer taking place solely at one end or both ends of the polymer backbone, i.e. not in the side or lateral chains
Definitions
- the present invention relates to copolymers of conjugated diene and monoolefin, which copolymer bears at least one functional group, as well as their method of preparation.
- the modification of already known polymers can consist of a post-polymerization modification, modification which takes place on the polymer synthesized beforehand, such as for example the hydrogenation reaction or the grafting of function along the polymer chain, in the copolymerization of a functional monomer, in the use of a functionalizing agent in the polymer chain termination reaction or in the polymer chain initiation reaction.
- This process which uses a functional transfer agent not only allows the synthesis of copolymer of conjugated diene and monoolefin, which copolymer bears a function on one end of the copolymer chain, but also opens the way to the synthesis of copolymers of conjugated diene and telechelic or hetero-telechelic monoolefin.
- Another object of the invention is a process for preparing the copolymer in accordance with the invention.
- the invention also relates to a compound of formula (II), intermediate compound in the synthesis of the copolymer in accordance with the invention, Y(A-(CH 2 ) d -B1) y (II) in which Y, d, y, A and B1 are as previously defined.
- the invention also relates to a rubber composition comprising the copolymer in accordance with the invention.
- any interval of values denoted by the expression “between a and b” represents the range of values greater than “a” and less than “b” (that is to say limits a and b excluded) while any interval of values denoted by the expression “from a to b” means the range of values going from “a” to "b” (that is to say including the strict limits a and b).
- composition comprising the mixture and/or the in situ reaction product of the various constituents used, some of these basic constituents (for example the elastomer, the filler or other additive conventionally used in a rubber composition intended for the manufacture of tires) being capable of, or intended to react with each other, at least in part, during the various phases of manufacture of the composition intended for the manufacture of tires.
- the copolymer in accordance with the invention has the essential characteristic of comprising a copolymer chain A.
- the copolymer chain A comprises monomer units M1 and monomer units M2, M1 being a conjugated diene and M2 being ethylene or a mixture of ethylene and an ⁇ -monoolefin.
- M1 being a conjugated diene
- M2 being ethylene or a mixture of ethylene and an ⁇ -monoolefin.
- the respective molar percentage of monomer units M1 and monomer units M2 in the copolymer chain A is strictly greater than 0.
- the monomer units M1 result from the insertion of the monomer M1, a conjugated diene, in the growing copolymer chain A, in particular by a 1,2 or 1,4 addition.
- a conjugated diene is meant one or more conjugated dienes.
- the monomer units M1 designate the monomer units resulting from the insertion of each of the conjugated dienes.
- the M2 monomer units result from the insertion of the M2 monomer into the growing copolymer A chain.
- the term “an” ⁇ -monoolefin is understood to mean one or more ⁇ -monoolefins.
- the monomer units M2 designate the monomer units resulting from the insertion of each of the monomers of the monomer mixture.
- conjugated diene By way of conjugated diene, mention may be made of 1,3-dienes, particularly a conjugated diene chosen from the group consisting of 1,3-butadiene, isoprene and their mixture. Preferably M1 is 1,3-butadiene.
- ⁇ -monoolefin suitable are aliphatic or aromatic ⁇ -monoolefins, particularly aliphatic ⁇ -monoolefins preferably having 3 to 18 carbon atoms such as propene, 1-butene, 1-hexene, 1-octene, 1-hexadecene or mixtures thereof.
- the monomer units M1 represent more than 40%, preferably more than 60% by mole of the monomer units of the copolymer.
- the monomer units M1 represent less than 35% by mole of the monomer units of the copolymer.
- the ethylene units represent more than 50%, preferably more than 65% by mole of the monomer units of the copolymer.
- the monomer units M1 contain more than 80% by mole of unit resulting from a 1,4-trans insertion of M1 in the copolymer chain.
- the copolymer preferably contains less than 0.5% by mole of aliphatic hydrocarbon-based cyclic units, more preferably is devoid of such units, the cyclic unit containing a cycle with 5 or 6 carbon atoms.
- the copolymer in accordance with the invention is a copolymer of M1 and of M2, in particular a copolymer of 1,3-butadiene and ethylene or a terpolymer of 1,3-butadiene, ethylene and an ⁇ -monoolefin as defined above.
- the copolymer preferably has a number-average molar mass (Mn) of at least 5000 g/mol, more preferably of at least 60,000 g/mol, a particularly advantageous minimum value for use of the copolymer as an elastomer, for example in a rubber composition for tires.
- Mn number-average molar mass
- its number-average molar mass does not exceed 1,500,000 g/mol; beyond this value the viscosity of the copolymer can make the use of the copolymer tricky.
- It preferably has a polydispersity index ⁇ equal to Mw/Mn (Mw being the weight-average molar mass) of between 1.20 and 3.00.
- Mn, Mw and ⁇ are measured according to the method described in paragraph II.1.
- the copolymer chain A has the other essential characteristic of carrying a function B at the end.
- the function B can be attached to the copolymer chain directly by a covalent bond or via a divalent group of formula (I) -(CH 2 ) w - (I) in which w is an integer from 1 to 50, preferably from 1 to 11.
- w is equal to 3.
- Function B is chosen from the group consisting of functions B1 and B2.
- B1 is selected from the group consisting of N(SiMe 3 ) 2 ; N(SiMe 2 CH 2 CH 2 SiMe 2 ); para-C 6 H 4 (NMe 2 ); para-C 6 H 4 (OMe); para-C 6 H 4 (N(SiMe 3 ) 2 ); ortho-CH 2 -C 6 H 4 NMe 2 ; ortho-CH 2 -C 6 H 4 OMe; C6F5 ; C3F7 ; C6F13 ; CH(OCH 2 CH 2 O).
- B2 is a function deriving from B1.
- function deriving from B1 is meant a function which is obtained by modification of the function B1 according to the reactions known to those skilled in the art.
- Function B1 is advantageously the N(SiMe 2 CH 2 CH 2 SiMe 2 ) group or the N(SiMe 3 ) 2 group.
- Function B2 is advantageously chosen from the group consisting of amines, ammoniums and ketones. When B2 is an amine, it is typically obtained by deprotection of the N(SiMe 2 CH 2 CH 2 SiMe 2 ) group or of the N(SiMe 3 ) 2 group, optionally followed by an alkylation, according to reactions well known to those skilled in the art.
- B2 When B2 is an ammonium, it can be obtained by modification of the same N(SiMe 2 CH 2 CH 2 SiMe 2 ) or N(SiMe 3 ) 2 groups, for example by quaternization reaction according to methods well known to those skilled in the art.
- B2 When B2 is a ketone, it is advantageously obtained by deprotection of the acetal function CH(OCH 2 CH 2 O), a process also well known to those skilled in the art.
- B2 is a primary, secondary or tertiary amine, preferably a primary amine.
- function B is function B1.
- the copolymer carries a second function, Z function.
- the Z function is preferably carried on one chain end of the copolymer A.
- the copolymer carries a B function and a Z function both at the end of the chain, the two functions are carried respectively by different ends: the copolymer is said to be telechelic or heterotelechelic in the particular case where Z is different from B.
- the function Z is preferably chosen from halogens, groups comprising an unsaturated carbon-carbon bond and functions containing a heteroatom chosen from S, N, Si, O, B and P.
- the copolymer is preferably linear.
- copolymer in accordance with the invention can be prepared by the process described below.
- step (b) is a reaction of the compound of formula (II) with a compound comprising an acid proton, called a stopper (or stopper).
- a stopper a compound comprising an acid proton
- carboxylic acids in particular C 2 -C 18 fatty acids such as acetic acid, stearic acid, aliphatic or aromatic alcohols, such as methanol, ethanol, isopropanol, phenolic antioxidants, primary or secondary amines such as antioxidants comprising the diaminophenylene unit.
- This variant of the process makes it possible to synthesize a copolymer comprising a monofunctional copolymer chain, since the copolymer chain A of the copolymer bears the function B1 at the end of the chain provided by step (a) of the process.
- step (b) is a reaction of the compound of formula (II) with a functionalizing agent.
- the functionalization reaction involves the breaking of the bond formed by Y and the carbon both adjacent to Y and belonging to the copolymer chain A.
- the functionalization agent is chosen by the person skilled in the art for its reactivity vis-à-vis this bond and for the chemical nature of the Z function that it carries.
- Step (b) then being a functionalization reaction, the method allows access according to this other variant to a telechelic or hetero-telechelic copolymer, since one end of the copolymer chain A carries the B1 function provided by step (a), and the other end the Z function provided by step (b).
- the termination reaction is carried out by bringing the polymerization reaction medium into contact with a termination agent, whether it is a stopper or a functionalizing agent, at a monomer conversion rate chosen by the person skilled in the art according to the desired macrostructure of the copolymer.
- Step (c) is an optional step depending on whether or not it is desired to transform function B1, in particular into function B2.
- the embodiment of the method which comprises step (c) can be applied to the two variants of the method described previously.
- step (c) can be carried out simultaneously with step (b).
- step (b) and (c) are concomitant, mention may be made of the case where step (b) is a termination reaction with an acid compound and step (c) is a deprotection reaction of the B1 function under acidic conditions.
- step (c) is a reaction for deprotection of the function B1 in B2, carried out in an acidic or basic medium depending on the chemical nature of the function B1 to be deprotected.
- the trimethylsilyl group which protects the amine function can be hydrolyzed in an acidic or basic medium.
- the choice of the conditions of deprotection is done judiciously by a person skilled in the art, taking into account the chemical structure of the substrate to be deprotected.
- copolymer prepared according to the process in accordance with the invention can be separated from the reaction medium of step (b) or (c) according to processes well known to those skilled in the art, for example by an operation of evaporation of the solvent under reduced pressure or by a steam stripping operation.
- Step (a) of the process in accordance with the invention requires the preparation of the compound of formula (II).
- the compound of formula (II) is prepared by the copolymerization of a monomer mixture containing the monomer M1 and the monomer M2 in the presence of a catalytic system comprising a transfer agent of formula (III) and a metallocene catalyst, Y((CH 2 ) d B1) y (III)
- Y, B1, d and y being as defined previously, in particular in the various described embodiments of the invention.
- copolymerization of a monomer mixture containing a conjugated diene and a monoolefin such as ethylene, an ⁇ -monoolefin or their mixture can be carried out in accordance with patent applications EP1 092 731 , WO 2004035639 , WO2005028526 , WO 2007054223 And WO 2007054224 . knowing that the co-catalyst of the catalytic systems described in these documents is replaced in the present case by the transfer agent. Furthermore, those skilled in the art adapt the polymerization conditions described in these documents so as to achieve the desired microstructure and macrostructure of the copolymer chain A.
- the molar ratio of the transfer agent to the metal Met constituting the metallocene catalyst is preferably within a range ranging from 1 to 100, more preferably is greater than or equal to 1 and less than 10.
- the range of values ranging from 1 to less than 10 is in particular more favorable for obtaining copolymers of high molar masses.
- a person skilled in the art adapts the polymerization conditions and the concentrations of each of the reagents (constituents of the catalytic system, monomers, stopper), according to the equipment (tools, reactors) used to carry out the polymerization and the various chemical reactions.
- the copolymerization as well as the handling of the monomers, of the catalytic system and of the polymerization solvent(s) take place under anhydrous conditions and under an inert atmosphere.
- Polymerization solvents are typically hydrocarbon, aliphatic or aromatic solvents.
- the monomer M1 is preferably a monomer chosen from the group consisting of 1,3-butadiene, isoprene and their mixture, more preferably is 1,3-butadiene.
- the monomer M2 is ethylene or a mixture of ethylene and an ⁇ -monoolefin.
- Suitable ⁇ -monoolefins are those mentioned above, namely aliphatic or aromatic ⁇ -monoolefins, particularly aliphatic ⁇ -monoolefins preferably having 3 to 18 carbon atoms such as propene, 1-butene, 1-hexene, 1-octene, 1-hexadecene or mixtures thereof.
- the transfer agent is preferably of formula (III-a) or (III-b), with d ranging from 1 to 11, preferably being equal to 3.
- d is equal to 3 is advantageous in particular from the point of view of the accessibility of the transfer agent, since the reagent necessary for its synthesis is a commercial product or a product which is also easily accessible by synthesis.
- the transfer agent can be prepared by reaction of the metallic form of Y, called reactive, with a substrate of formula X-(CH 2 ) d -B1, B1 and d being as defined previously, X being a halogen, preferably a bromine atom.
- the transfer agent of formula (III) is preferably prepared by reaction of AlCl 3 with a derivative of a compound of formula X-(CH 2 ) d -B1 described above, this derivative possibly being an ionic salt based on lithium or potassium, for example of the respective formula Li(CH 2 ) d -B1 or K(CH 2 ) d -B1 or their form complexed with a solvent, as is well known in organometallic compounds based on lithium or potassium.
- the transfer agent is typically synthesized under operating conditions generally used in the synthesis of organometallic compounds, that is to say under anhydrous conditions and under an inert atmosphere, in ether solvents, by a controlled addition of a solution of the substrate, such as a drop by drop, to the reagent in suspension in the solvent.
- the transfer agent is recovered in a manner known per se, for example by evaporation of the synthesis solvent or by recrystallization from a solvent or a mixture of solvents.
- the metallocene catalyst is a metallocene comprising the unit (in English “moiety”) of formula (IV-1) P(Cp 1 )(Cp 2 )Met (IV-1)
- Met being a group 4 metal atom or a rare earth metal atom, Cp 1 and Cp 2 , identical or different, being chosen from the group consisting of cyclopentadienyl groups, indenyl groups and fluorenyl groups, the groups possibly being substituted or not,
- P being a group bridging the two groups Cp 1 and Cp 2 , and comprising at least one atom silicon or carbon.
- the Met atom is connected to a ligand molecule consisting of the two groups Cp 1 and Cp 2 linked together by the bridge P.
- the metallocene catalyst is a metallocene comprising the unit (in English “moiety”) of formula (IV-2) (Cp 1 )(Cp 2 )Met (IV-2)
- Met being a group 4 metal atom or a rare earth metal atom, Cp 1 and Cp 2 , identical or different, being chosen from the group consisting of cyclopentadienyl groups, indenyl groups and fluorenyl groups, the groups possibly being substituted or not.
- the rare earths are metals and designate the elements scandium, yttrium and the lanthanides whose atomic number varies from 57 to 71.
- substituted cyclopentadienyl, fluorenyl and indenyl groups mention may be made of those substituted by alkyl radicals having 1 to 6 carbon atoms or by aryl radicals having 6 to 12 carbon atoms.
- the choice of the radicals is also oriented by the accessibility to the corresponding molecules which are the substituted cyclopentadienes, fluorenes and indenes, because the latter are commercially available or easily synthesized.
- a bridged metallocene of formula (IV-1) as substituted cyclopentadienyl group, particular mention may be made of those substituted in position 2 or 3, such as tetramethylcyclopentadienyl or 3-trimethylsilylcyclopentadienyl groups.
- Position 2 (or 5) designates the position of the carbon atom which is adjacent to the carbon atom to which the P bridge is attached, as shown in the diagram below.
- Position 2 denotes the position of the carbon atom that is adjacent to the carbon atom to which the P bridge is attached, as shown in the diagram below.
- substituted cyclopentadienyl group mention may be made of 3-trimethylsilylcyclopentadienyl, tetramethylcyclopentadienyl; as a substituted indenyl group, mention may be made of methylindenyl and phenylindenyl groups; as substituted fluorenyl groups, mention may be made of the 2,7-ditertiobutyl-fluorenyl and 3,6-ditertiobutyl-fluorenyl groups.
- Cp 1 represents a substituted or unsubstituted cyclopentadienyl group and Cp 2 represents a substituted or unsubstituted fluorenyl group. More preferably, Cp 1 represents an unsubstituted cyclopentadienyl group and Cp 2 represents an unsubstituted fluorenyl group.
- the symbol P designated by the term bridge, corresponds to the formula MR 1 R 2 , M representing a silicon or carbon atom, preferably a silicon atom, R 1 and R 2 , identical or different, representing an alkyl group comprising from 1 to 20 carbon atoms. More preferably, the bridge P has the formula SiR 1 R 2 , R 1 and R 2 , being as defined previously. Even more preferentially, it corresponds to the formula SiMe 2 .
- the symbol Met preferably represents a rare earth metal atom, more preferably a lanthanide (Ln) atom whose atomic number ranges from 57 to 71, even more preferably a neodymium (Nd).
- the symbol Met preferably represents a lanthanide (Ln) atom whose atomic number ranges from 57 to 71, more preferably a neodymium atom (Nd).
- the metallocene can be in the form of crystallized powder or not, or even in the form of monocrystals.
- the metallocene can be present in a monomer or dimer form, these forms depending on the mode of preparation of the metallocene, as for example that is described in the applications WO 2007054223 And WO 2007054224 .
- the metallocene can be prepared conventionally by a process analogous to that described in the documents EP 1 092 731 , WO 2007054223 And WO 2007054224 , in particular by reaction under inert and anhydrous conditions of the salt of an alkali metal of the ligand with a rare earth salt such as a halide or a rare earth borohydride, or a salt of a group 4 metal in a suitable solvent, such as an ether, such as diethyl ether or tetrahydrofuran or any other solvent known to those skilled in the art.
- a suitable solvent such as an ether, such as diethyl ether or tetrahydrofuran or any other solvent known to those skilled in the art.
- the metallocene is separated from the reaction by-products by techniques known to those skilled in the art, such as filtration or precipitation in a second solvent.
- the metallocene is finally dried and isolated in solid form.
- Cp 1 represents a substituted or unsubstituted cyclopentadienyl group and Cp 2 represents a substituted or unsubstituted fluorenyl group. More preferably, Cp 1 represents an unsubstituted cyclopentadienyl group and Cp 2 represents an unsubstituted fluorenyl group.
- the unsubstituted fluorenyl group has the formula C 13 H 8 .
- the metallocene catalyst is preferably a lanthanide borohydride metallocene or a lanthanide halide metallocene, in particular a lanthanide chloride metallocene.
- Suitable ether is any ether which has the power to complex the alkali metal, in particular diethyl ether and tetrahydrofuran.
- the metallocene catalyst is of formula (IV-3a) or (IV-3b) or (IV-3c).
- [Me 2 Si(C 5 H 4 )(C 13 H 8 )NdCl] (IV-3a) [Me 2 Si(C 5 H 4 )(C 13 H 8 )Nd(BH 4 ) 2 Li(THF)]
- IV-3b) [Me 2 Si(C 5 H 4 )(C 13 H 8 )Nd(BH 4 )(THF)] (IV-3c)
- the compound of formula (II) is such that Y is Mg, B1 represents the N(SiMe 2 CH 2 CH 2 SiMe 2 ) group or the N(SiMe 3 ) 2 group and d ranges from 1 to 11 or equal to 3.
- the copolymer in accordance with the invention in particular when it is an elastomer, can be used in a rubber composition, in particular in a semi-finished product for a tire.
- the rubber composition in accordance with the invention may contain, in addition to the copolymer, any ingredient traditionally used in a rubber composition for tires, such as for example a reinforcing filler such as a carbon black or a silica, a plasticizing system, a crosslinking system, in particular vulcanization, one or more antioxidants.
- the SEC analyzes were carried out at high temperature (HT-SEC) using a Viscotek apparatus (from Malvern Instruments) equipped with 3 columns (PLgel Olexis 300 mm x 7 mm ID from Agilent Technologies) and 3 detectors (refractometer, viscometer and light scattering). 200 ⁇ L of a sample solution at a concentration of 5 mg mL -1 was eluted in 1,2,4-trichlorobenzene using a flow rate of 1 mL min -1 at 150°C. The mobile phase was stabilized with 2,6-di(tert-butyl)-4-methylphenol (200 mg L -1 ). OmniSEC software was used for data acquisition and analysis. The number-average molar masses Mn and the polydispersity index ⁇ were calculated by universal calibration using polystyrene standards.
- High-resolution NMR spectroscopy was performed on a Bruker DRX 400 spectrometer operating at 400 MHz for the proton and 101 MHz for the carbon-13.
- the acquisitions were made at 363 K using a 5 mm QNP probe for the 1 H and a 10 mm PSEX probe for the 13 C NMR.
- the samples were analyzed at a concentration of 5-15% by mass.
- a mixture of tetrachlorethylene (TCE) and deuterated benzene (C6D6) (2/1 v/v) was used as solvent.
- TCE tetrachlorethylene
- C6D6D6D6 deuterated benzene
- microstructure of ethylene/butadiene copolymers is determined by 13 C NMR according to the method described in Macromolecules 2001, 34, 6304-6311 .
- the 1-(3-bromopropyl)-2,2,5,5-tetramethyl-1-aza-2,5-disilacyclopentane magnesium solution is then recovered by cannulating this solution into a Schlenk tube under argon in order to remove the unreacted magnesium.
- This solution is then filtered under argon on Celite in order to recover MgR 2 in solution in THF. 100 mL of BuzO are added to this solution and the THF is distilled under vacuum at room temperature.
- the solution is transferred under an argon atmosphere into a 250 mL reactor.
- the argon is removed under vacuum and the reactor is pressurized to 4 bars using a gaseous mixture of ethylene/1,3-butadiene monomer of constant composition (5 molar % of 1,3-butadiene) at 70°C.
- the reactor is degassed after 2 h of polymerization and the temperature is brought back to 20°C.
- the polymerization medium is poured into a 1M methanol/HCl solution and is stirred for 1 hour.
- the precipitated polymer is solubilized in toluene and then is precipitated in a methanol solution in order to be washed in this way.
- the polymer is finally dried.
- composition of the copolymer is 95.6% mol of ethylene.
- 1,3-Butadiene is inserted at 24.7 mol% 1,4-trans, 11.0 mol% 1,2 and 64.3 mol% as rings.
- Example 2 The same procedure as Example 2 is followed for the synthesis of this copolymer but with a monomer mixture containing 20 mol% of 1,3-butadiene.
- composition of the copolymer is 80.0 mol% ethylene.
- 1,3-Butadiene is inserted at 19.0 mol% 1,4-trans, 44.5 mol% 1,2 and 36.5 mol% as rings.
- the composition of the copolymer is 80.1% mol of ethylene.
- the 1,3-butadiene is inserted at 17.5 mol% 1,4- trans, 45.2 mol% 1,2 and 37.3 mol% in the form of rings.
- Example 4 The same procedure as Example 4 is followed for the synthesis of this copolymer, but the polymerization this time lasts 4 hours.
- composition of the copolymer is 79.3% mol of ethylene.
- the 1,3-butadiene is inserted at 28.1% mol 1,4- trans, 38.7% mol 1,2 and 33.2% mol in the form of rings.
- composition of the copolymer is 75.3% mol of ethylene.
- the 1,3-butadiene is inserted at 25.7% mol 1,4-trans, 44.2% mol 1,2 and 30.1% mol in the form of rings.
- the argon is removed under vacuum and the reactor is pressurized to 4 bars by means of a gaseous mixture of ethylene/1,3-butadiene monomer of constant composition (20 molar % of 1,3-butadiene) at 80°C.
- the reactor is degassed after 90 minutes of polymerization and the temperature is brought back to 20°C.
- the polymerization medium is poured into a 1M methanol/HCl solution and is stirred for 1 hour.
- the precipitated polymer is re-solubilized in toluene, then is precipitated in a methanol solution to be washed in this way.
- the polymer is finally dried.
- step (c) being a hydrolysis reaction in a basic medium :
- Example 2 A fraction of the polymer of Example 2 is taken (10 g). The polymer is dissolved in toluene and then precipitated using a methanol/NaOH (1M) solution and stirred for 1 hour at room temperature.
- the polymer is recovered and then washed with methanol and dried under vacuum at 60°C.
- step (c) being a hydrolysis reaction in a basic medium :
- a fraction of the polymer of Example 3 is taken (8 g).
- the polymer is dissolved in toluene and then precipitated using a methanol/NaOH (1M) solution and stirred for 1 hour at room temperature.
- the polymer is recovered and then washed with methanol and dried under vacuum at 60°C.
- step (c) being a hydrolysis reaction in a basic medium :
- a fraction of the polymer of Example 4 is taken (7 g).
- the polymer is dissolved in toluene and then precipitated using a methanol/NaOH (1M) solution and stirred for 1 hour at room temperature.
- the polymer is recovered and then washed with methanol and dried under vacuum at 60°C.
- step (c) being a hydrolysis reaction in a basic medium :
- Example 5 A fraction of the polymer of Example 5 is taken (13 g). The polymer is dissolved in toluene and then precipitated using a methanol/NaOH (1M) solution and stirred for 1 hour at room temperature.
- the polymer is recovered and then washed with methanol and dried under vacuum at 60°C.
- step (c) being a hydrolysis reaction in a basic medium
- a fraction of the polymer of Example 6 is taken (3 g).
- the polymer is dissolved in toluene and then precipitated using a methanol/NaOH (1M) solution and stirred for 1 hour at room temperature.
- the polymer is recovered and then washed with methanol and dried under vacuum at 60°C.
- the solution is transferred under an argon atmosphere into a 250 mL reactor.
- the argon is removed under vacuum and the reactor is pressurized to 4 bars by means of a gaseous mixture of ethylene/1,3-butadiene monomer of constant composition (20% molar of 1,3-butadiene) at 70°C.
- the reactor is degassed after 2 h of polymerization and the temperature of the medium reaction is maintained at 70°C.
- a sample of 100 mL of the reaction medium is then taken. This sample is poured into a 1M methanol/HCl solution and is stirred for 1 hour. The precipitated reference polymer is solubilized in toluene and then is precipitated in a methanol solution in order to be washed in this way.
- the polymer is finally dried.
- the composition of the reference copolymer is 80.8% mol of ethylene.
- the 1,3-butadiene is inserted at 18.7% mol 1,4- trans, 39.9% mol 1,2 and 41.4% mol in the form of rings.
- the temperature is brought back to 20°C.
- the polymerization medium is poured into a 1M methanol/HCl solution and is stirred for 1 hour.
- the precipitated polymer is solubilized in toluene and then is precipitated in a methanol solution in order to be washed in this way.
- the polymer is finally dried.
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Polymerisation Methods In General (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
Description
La présente invention concerne des copolymères de diène conjugué et de monooléfine, lequel copolymère porte au moins un groupe fonctionnel, ainsi que leur procédé de préparation.The present invention relates to copolymers of conjugated diene and monoolefin, which copolymer bears at least one functional group, as well as their method of preparation.
Il est toujours d'intérêt d'avoir à disposition de nouveaux polymères afin d'élargir la gamme de matériaux déjà disponibles et améliorer les fonctionnalités des matériaux déjà existants. Généralement, le développement de nouveaux polymères est motivé pour améliorer les performances des matériaux déjà existants.It is always of interest to have new polymers available in order to broaden the range of materials already available and improve the functionalities of already existing materials. Generally, the development of new polymers is motivated to improve the performance of already existing materials.
Parmi les voies d'accès à de nouveaux polymères, on peut citer la modification de polymères déjà connus. La modification de polymères déjà connus peut consister en une modification post-polymérisation, modification qui a lieu sur le polymère au préalable synthétisé, comme par exemple la réaction d'hydrogénation ou le greffage de fonction le long de la chaîne polymère, en la copolymérisation d'un monomère fonctionnel, en l'utilisation d'un agent de fonctionnalisation dans la réaction de terminaison de la chaîne polymère ou dans la réaction d'amorçage de la chaîne polymère.Among the access routes to new polymers, mention may be made of the modification of already known polymers. The modification of already known polymers can consist of a post-polymerization modification, modification which takes place on the polymer synthesized beforehand, such as for example the hydrogenation reaction or the grafting of function along the polymer chain, in the copolymerization of a functional monomer, in the use of a functionalizing agent in the polymer chain termination reaction or in the polymer chain initiation reaction.
Les Demanderesses ont déjà mis au point la synthèse de copolymères de diène conjugué et de monooléfine, décrite par exemple dans les demandes de brevet
Ainsi, un premier objet de l'invention est un copolymère comprenant une chaîne copolymère A portant une fonction B choisie dans le groupe constitué par les fonctions B1 et B2,
- la chaîne copolymère A étant une chaîne copolymère comprenant des unités monomères M1 et des unités monomères M2, M1 étant un diène conjugué,
- B1 étant choisie dans le groupe constitué par N(SiMe3)2 ; N(SiMe2CH2CH2SiMe2) ; para-C6H4(NMe2); para-C6H4(OMe) ; para-C6H4(N(SiMe3)2) ; ortho-CH2-C6H4NMe2 ; ortho-CH2-C6H4OMe ; C6F5 ; C3F7 ; C6F13 ; CH(OCH2CH2O) ;
- B2 étant une fonction dérivant de B1.
- la fonction B étant portée en extrémité de la chaîne copolymère A,
- M2 étant l'éthylène ou un mélange d'éthylène et d'une α-monooléfine.
- the copolymer chain A being a copolymer chain comprising monomer units M1 and monomer units M2, M1 being a conjugated diene,
- B1 being chosen from the group consisting of N(SiMe 3 ) 2 ; N(SiMe 2 CH 2 CH 2 SiMe 2 ); para-C 6 H 4 (NMe 2 ); para-C 6 H 4 (OMe); para-C 6 H 4 (N(SiMe 3 ) 2 ); ortho-CH 2 -C 6 H 4 NMe 2 ; ortho-CH 2 -C 6 H 4 OMe; C6F5 ; C3F7 ; C6F13 ; CH(OCH 2 CH 2 O);
- B2 being a function deriving from B1.
- the function B being carried at the end of the copolymer chain A,
- M2 being ethylene or a mixture of ethylene and an α-monoolefin.
Un autre objet de l'invention est un procédé pour préparer le copolymère conforme à l'invention.Another object of the invention is a process for preparing the copolymer in accordance with the invention.
Un objet décrit par la présente est l'utilisation d'un agent de transfert de formule (III) dans la synthèse de copolymère conforme à l'invention,
Y((CH2)dB1)y (III)
- ∘ y étant égal à 2 ou 3,
- ∘ lorsque y = 2, le symbole Y étant un alcalino-terreux ou le zinc, et lorsque y = 3, Y étant l'aluminium ;
- ∘ d étant un nombre entier de 0 à 50, avantageusement de 0 à 11 ;
- ∘ B1 étant choisi dans le groupe constitué par N(SiMe3)2; N(SiMe2CH2CH2SiMe2); para-C6H4(NMe2); para-C6H4(OMe); para-C6H4(N(SiMe3)2); ortho-CH2-C6H4NMe2; ortho-CH2-C6H4OMe; C6F5; C3F7; C6F13; CH(OCH2CH2O).
Y((CH 2 ) d B1) y (III)
- ∘ y being equal to 2 or 3,
- ∘ when y = 2, the symbol Y being an alkaline earth metal or zinc, and when y = 3, Y being aluminum;
- ∘ d being an integer from 0 to 50, advantageously from 0 to 11;
- ∘ B1 being chosen from the group consisting of N(SiMe 3 ) 2 ; N(SiMe 2 CH 2 CH 2 SiMe 2 ); para-C 6 H 4 (NMe 2 ); para-C 6 H 4 (OMe); para-C 6 H 4 (N(SiMe 3 ) 2 ); ortho-CH 2 -C 6 H 4 NMe 2 ; ortho-CH 2 -C 6 H 4 OMe; C6F5 ; C3F7 ; C6F13 ; CH(OCH 2 CH 2 O).
L'invention concerne aussi un composé de formule (II), composé intermédiaire dans la synthèse du copolymère conforme à l'invention,
Y(A-(CH2)d-B1)y (II)
dans laquelle Y, d, y, A et B1 sont tels que définis précédemment.The invention also relates to a compound of formula (II), intermediate compound in the synthesis of the copolymer in accordance with the invention,
Y(A-(CH 2 ) d -B1) y (II)
in which Y, d, y, A and B1 are as previously defined.
L'invention porte également sur une composition de caoutchouc comprenant le copolymère conforme à l'invention.The invention also relates to a rubber composition comprising the copolymer in accordance with the invention.
Tout intervalle de valeurs désigné par l'expression "entre a et b" représente le domaine de valeurs supérieur à "a" et inférieur à "b" (c'est-à-dire bornes a et b exclues) tandis que tout intervalle de valeurs désigné par l'expression "de a à b" signifie le domaine de valeurs allant de "a" jusqu'à "b" (c'est-à-dire incluant les bornes strictes a et b).Any interval of values denoted by the expression "between a and b" represents the range of values greater than "a" and less than "b" (that is to say limits a and b excluded) while any interval of values denoted by the expression "from a to b" means the range of values going from "a" to "b" (that is to say including the strict limits a and b).
Par l'expression composition "à base de", il faut entendre dans la présente description une composition comportant le mélange et/ou le produit de réaction in situ des différents constituants utilisés, certains de ces constituants de base (par exemple l'élastomère, la charge ou autre additif classiquement utilisé dans une composition de caoutchouc destinée à la fabrication de pneumatique) étant susceptibles de, ou destinés à réagir entre eux, au moins en partie, lors des différentes phases de fabrication de la composition destinée à la fabrication de pneumatique.By the expression "based on" composition, it is meant in the present description a composition comprising the mixture and/or the in situ reaction product of the various constituents used, some of these basic constituents (for example the elastomer, the filler or other additive conventionally used in a rubber composition intended for the manufacture of tires) being capable of, or intended to react with each other, at least in part, during the various phases of manufacture of the composition intended for the manufacture of tires.
Le copolymère conforme à l'invention a pour caractéristique essentielle de comprendre une chaîne copolymère A. La chaîne copolymère A comprend des unités monomères M1 et des unités monomères M2, M1 étant un diène conjugué et M2 étant l'éthylène ou un mélange d'éthylène et d'une α-monooléfine. Par définition, le pourcentage molaire respectif des unités monomères M1 et des unités monomères M2 dans la chaîne copolymère A est strictement supérieur à 0.The copolymer in accordance with the invention has the essential characteristic of comprising a copolymer chain A. The copolymer chain A comprises monomer units M1 and monomer units M2, M1 being a conjugated diene and M2 being ethylene or a mixture of ethylene and an α-monoolefin. By definition, the respective molar percentage of monomer units M1 and monomer units M2 in the copolymer chain A is strictly greater than 0.
Les unités monomères M1 résultent de l'insertion du monomère M1, un diène conjugué, dans la chaîne copolymère A en croissance, notamment par une addition 1,2 ou 1,4. On entend par « un » diène conjugué un ou plusieurs diènes conjugués. Dans le cas où M1 représente un mélange de diènes conjugués, les unités monomères M1 désignent les unités monomères résultant de l'insertion de chacun des diènes conjugués.The monomer units M1 result from the insertion of the monomer M1, a conjugated diene, in the growing copolymer chain A, in particular by a 1,2 or 1,4 addition. By “a” conjugated diene is meant one or more conjugated dienes. In the case where M1 represents a mixture of conjugated dienes, the monomer units M1 designate the monomer units resulting from the insertion of each of the conjugated dienes.
Les unités monomères M2 résultent de l'insertion du monomère M2 dans la chaîne copolymère A en croissance. On entend par « une » α-monooléfine une ou plusieurs α-monooléfines. Dans le cas où M2 représente un mélange monomère, c'est à dire un mélange de plusieurs monomères, les unités monomères M2 désignent les unités monomères résultant de l'insertion de chacun des monomères du mélange monomère.The M2 monomer units result from the insertion of the M2 monomer into the growing copolymer A chain. The term “an” α-monoolefin is understood to mean one or more α-monoolefins. In the case where M2 represents a monomer mixture, that is to say a mixture of several monomers, the monomer units M2 designate the monomer units resulting from the insertion of each of the monomers of the monomer mixture.
A titre de diène conjugué, on peut citer les 1,3-diènes, particulièrement un diène conjugué choisi dans groupe constitué par le 1,3-butadiène, l'isoprène et leur mélange. De préférence M1 est le 1,3-butadiène.By way of conjugated diene, mention may be made of 1,3-dienes, particularly a conjugated diene chosen from the group consisting of 1,3-butadiene, isoprene and their mixture. Preferably M1 is 1,3-butadiene.
A titre d'α-monooléfine, conviennent les α-monooléfines aliphatiques ou aromatiques, particulièrement les α-monooléfines aliphatiques ayant de préférence 3 à 18 atomes de carbone telles que le propène, le 1-butène, le 1-hexène, le 1-octène, le 1-hexadécène ou leurs mélanges.As α-monoolefin, suitable are aliphatic or aromatic α-monoolefins, particularly aliphatic α-monoolefins preferably having 3 to 18 carbon atoms such as propene, 1-butene, 1-hexene, 1-octene, 1-hexadecene or mixtures thereof.
Selon un mode de réalisation de l'invention, les unités monomères M1 représentent plus de 40%, préférentiellement plus de 60% en mole des unités monomères du copolymère.According to one embodiment of the invention, the monomer units M1 represent more than 40%, preferably more than 60% by mole of the monomer units of the copolymer.
Selon un autre mode de réalisation de l'invention, les unités monomères M1 représentent moins de 35% en mole des unités monomères du copolymère.According to another embodiment of the invention, the monomer units M1 represent less than 35% by mole of the monomer units of the copolymer.
Selon un mode de réalisation particulier de l'invention, les unités éthylène représentent plus de 50%, préférentiellement plus de 65% en mole des unités monomères du copolymère.According to a particular embodiment of the invention, the ethylene units represent more than 50%, preferably more than 65% by mole of the monomer units of the copolymer.
Selon un mode de réalisation préférentiel de l'invention, les unités monomères M1 contiennent plus de 80% en mole de motif résultant d'une insertion 1,4-trans de M1 dans la chaîne copolymère.According to a preferred embodiment of the invention, the monomer units M1 contain more than 80% by mole of unit resulting from a 1,4-trans insertion of M1 in the copolymer chain.
Selon l'un quelconque des modes de réalisation de l'invention, le copolymère contient de préférence moins de 0,5% en mole de motifs cycliques hydrocarbonés aliphatiques, de manière plus préférentielle est dépourvu de tels motifs, le motif cyclique contenant un cycle à 5 ou 6 atomes de carbone.According to any one of the embodiments of the invention, the copolymer preferably contains less than 0.5% by mole of aliphatic hydrocarbon-based cyclic units, more preferably is devoid of such units, the cyclic unit containing a cycle with 5 or 6 carbon atoms.
Selon un mode de réalisation avantageux de l'invention, le copolymère conforme à l'invention est un copolymère de M1 et de M2, notamment un copolymère de 1,3-butadiène et d'éthylène ou un terpolymère de 1,3-butadiène, d'éthylène et d'une α-monooléfine telle que définie précédemment.According to an advantageous embodiment of the invention, the copolymer in accordance with the invention is a copolymer of M1 and of M2, in particular a copolymer of 1,3-butadiene and ethylene or a terpolymer of 1,3-butadiene, ethylene and an α-monoolefin as defined above.
Selon l'un quelconque des modes de réalisation de l'invention, le copolymère présente de préférence une masse molaire moyenne en nombre (Mn) d'au moins 5000 g/mol, de manière plus préférentielle d'au moins 60 000 g/mol, valeur minimum particulièrement avantageuse pour un usage du copolymère en tant qu'élastomère par exemple dans une composition de caoutchouc pour pneumatique. Généralement, sa masse molaire moyenne en nombre n'excède pas 1500 000 g/mol ; au-delà de cette valeur la viscosité du copolymère peut rendre l'utilisation du copolymère délicate. Il présente de préférence un indice de polydispersité Ð, égal à Mw/Mn (Mw étant la masse molaire moyenne en poids) compris entre 1,20 et 3,00. Les valeurs de Mn, Mw et Ð sont mesurées selon la méthode décrite dans le paragraphe II.1.According to any one of the embodiments of the invention, the copolymer preferably has a number-average molar mass (Mn) of at least 5000 g/mol, more preferably of at least 60,000 g/mol, a particularly advantageous minimum value for use of the copolymer as an elastomer, for example in a rubber composition for tires. Generally, its number-average molar mass does not exceed 1,500,000 g/mol; beyond this value the viscosity of the copolymer can make the use of the copolymer tricky. It preferably has a polydispersity index λ equal to Mw/Mn (Mw being the weight-average molar mass) of between 1.20 and 3.00. The values of Mn, Mw and Ð are measured according to the method described in paragraph II.1.
La chaîne copolymère A a pour autre caractéristique essentielle de porter une fonction B en extrémité. La fonction B peut être attachée à la chaîne copolymère directement par une liaison covalente ou par l'intermédiaire d'un groupe divalent de formule (I)
-(CH2)w- (I)
dans laquelle w est un nombre entier de 1 à 50, préférentiellement de 1 à 11. Avantageusement w est égal à 3.The copolymer chain A has the other essential characteristic of carrying a function B at the end. The function B can be attached to the copolymer chain directly by a covalent bond or via a divalent group of formula (I)
-(CH 2 ) w - (I)
in which w is an integer from 1 to 50, preferably from 1 to 11. Advantageously w is equal to 3.
La fonction B est choisie dans le groupe constitué par les fonctions B1 et B2. B1 est choisie dans le groupe constitué par N(SiMe3)2; N(SiMe2CH2CH2SiMe2); para-C6H4(NMe2); para-C6H4(OMe); para-C6H4(N(SiMe3)2); ortho-CH2-C6H4NMe2; ortho-CH2-C6H4OMe; C6F5; C3F7; C6F13; CH(OCH2CH2O). B2 est une fonction dérivant de B1.Function B is chosen from the group consisting of functions B1 and B2. B1 is selected from the group consisting of N(SiMe 3 ) 2 ; N(SiMe 2 CH 2 CH 2 SiMe 2 ); para-C 6 H 4 (NMe 2 ); para-C 6 H 4 (OMe); para-C 6 H 4 (N(SiMe 3 ) 2 ); ortho-CH 2 -C 6 H 4 NMe 2 ; ortho-CH 2 -C 6 H 4 OMe; C6F5 ; C3F7 ; C6F13 ; CH(OCH 2 CH 2 O). B2 is a function deriving from B1.
On entend par fonction dérivant de B1 une fonction qui est obtenue par modification de la fonction B1 selon les réactions connues de l'homme du métier.By function deriving from B1 is meant a function which is obtained by modification of the function B1 according to the reactions known to those skilled in the art.
La fonction B1 est avantageusement le groupe N(SiMe2CH2CH2SiMe2) ou le groupe N(SiMe3)2. La fonction B2 est avantageusement choisie dans le groupe constitué par les amines, les ammoniums et les cétones. Lorsque B2 est une amine, elle est obtenue typiquement par déprotection du groupe N(SiMe2CH2CH2SiMe2) ou du groupe N(SiMe3)2 , éventuellement suivie par une alkylation, selon des réactions bien connues de l'homme du métier. Lorsque B2 est un ammonium, elle peut être obtenue par modification des mêmes groupes N(SiMe2CH2CH2SiMe2) ou N(SiMe3)2 , par exemple par réaction de quaternisation selon des procédés bien connus de l'homme du métier. Lorsque B2 est une cétone, elle est obtenue avantageusement par déprotection de la fonction acétal CH(OCH2CH2O), procédé également bien connu de l'homme du métier.Function B1 is advantageously the N(SiMe 2 CH 2 CH 2 SiMe 2 ) group or the N(SiMe 3 ) 2 group. Function B2 is advantageously chosen from the group consisting of amines, ammoniums and ketones. When B2 is an amine, it is typically obtained by deprotection of the N(SiMe 2 CH 2 CH 2 SiMe 2 ) group or of the N(SiMe 3 ) 2 group, optionally followed by an alkylation, according to reactions well known to those skilled in the art. When B2 is an ammonium, it can be obtained by modification of the same N(SiMe 2 CH 2 CH 2 SiMe 2 ) or N(SiMe 3 ) 2 groups, for example by quaternization reaction according to methods well known to those skilled in the art. When B2 is a ketone, it is advantageously obtained by deprotection of the acetal function CH(OCH 2 CH 2 O), a process also well known to those skilled in the art.
Selon un mode de réalisation préférentiel de l'invention, B2 est une amine, primaire, secondaire ou tertiaire, de préférence une amine primaire.According to a preferred embodiment of the invention, B2 is a primary, secondary or tertiary amine, preferably a primary amine.
Selon un mode de réalisation particulier de l'invention, la fonction B est la fonction B1.According to a particular embodiment of the invention, function B is function B1.
Selon une variante de l'invention, le copolymère porte une deuxième fonction, fonction Z. La fonction Z est portée de préférence sur une extrémité de chaîne du copolymère A. Lorsque le copolymère porte une fonction B et une fonction Z toutes les deux en extrémité de chaîne, les deux fonctions sont portées respectivement par des extrémités différentes : le copolymère est dit téléchélique ou hétérotéléchélique dans le cas particulier où Z est différent de B.According to a variant of the invention, the copolymer carries a second function, Z function. The Z function is preferably carried on one chain end of the copolymer A. When the copolymer carries a B function and a Z function both at the end of the chain, the two functions are carried respectively by different ends: the copolymer is said to be telechelic or heterotelechelic in the particular case where Z is different from B.
Selon l'un quelconque des modes de réalisation de cette variante, la fonction Z est de préférence choisie parmi les halogènes, les groupes comportant une liaison insaturée carbone-carbone et les fonctions contenant un hétéroatome choisi parmi S, N, Si, O, B et P.According to any one of the embodiments of this variant, the function Z is preferably chosen from halogens, groups comprising an unsaturated carbon-carbon bond and functions containing a heteroatom chosen from S, N, Si, O, B and P.
Selon l'un quelconque des modes de réalisation de l'invention, le copolymère est préférentiellement linéaire.According to any one of the embodiments of the invention, the copolymer is preferably linear.
Le copolymère conforme à l'invention peut être préparé par le procédé décrit ci-après.The copolymer in accordance with the invention can be prepared by the process described below.
Le procédé pour préparer le copolymère a pour caractéristique essentielle de comprendre les étapes (a) et (b), et le cas échéant l'étape (c) suivantes :
- (a) la préparation d'un composé de formule (II)
Y(A-(CH2)d-B1)y (II)
dans laquelle- ∘ y est égal à 2 ou 3,
- ∘ lorsque y = 2, le symbole Y est un alcalino-terreux ou le zinc, et lorsque y = 3, Y est l'aluminium ;
- ∘ d est un nombre entier de 0 à 50, avantageusement de 0 à 11;
- ∘ le symbole A représentant la chaîne copolymère A décrite précédemment ;
- ∘ B1 est choisi dans le groupe constitué par N(SiMe3)2; N(SiMe2CH2CH2SiMe2); para-C6H4(NMe2); para-C6H4(OMe); para-C6H4(N(SiMe3)2); ortho-CH2-C6H4NMe2; ortho-CH2-C6H4OMe; C6F5; C3F7; C6F13; CH(OCH2CH2O)
- (b) une réaction de terminaison de la chaîne copolymère A,
- (c) une réaction de modification de la fonction B1, notamment pour former la fonction B2.
- (a) the preparation of a compound of formula (II)
Y(A-(CH 2 ) d -B1) y (II)
in which- ∘ y is equal to 2 or 3,
- ∘ when y = 2, the symbol Y is alkaline earth or zinc, and when y = 3, Y is aluminum;
- ∘ d is an integer from 0 to 50, advantageously from 0 to 11;
- ∘ the symbol A representing the copolymer chain A described above;
- ∘ B1 is chosen from the group consisting of N(SiMe 3 ) 2 ; N(SiMe 2 CH 2 CH 2 SiMe 2 ); para-C 6 H 4 (NMe 2 ); para-C 6 H 4 (OMe); para-C 6 H 4 (N(SiMe 3 ) 2 ); ortho-CH 2 -C 6 H 4 NMe 2 ; ortho-CH 2 -C 6 H 4 OMe; C6F5 ; C3F7 ; C6F13 ; CH(OCH 2 CH 2 O)
- (b) a copolymer A chain termination reaction,
- (c) a modification reaction of function B1, in particular to form function B2.
Selon une variante du procédé, l'étape (b) est une réaction du composé de formule (II) avec un composé comportant un proton acide, dit stoppeur (ou agent de stoppage). A titre de stoppeur, on peut citer l'eau, les acides carboxyliques notamment les acides gras en C2-C18 comme l'acide acétique, l'acide stéarique, les alcools aliphatiques ou aromatiques, comme le méthanol, l'éthanol, l'isopropanol, des antioxydants phénoliques, des amines primaires ou secondaires comme des antioxydants comportant le motif diaminophénylène. Cette variante du procédé permet de synthétiser un copolymère comprenant une chaîne copolymère monofonctionnelle, puisque la chaîne copolymère A du copolymère porte la fonction B1 en extrémité de chaîne apportée par l'étape (a) du procédé.According to a variant of the process, step (b) is a reaction of the compound of formula (II) with a compound comprising an acid proton, called a stopper (or stopper). As a stopper, mention may be made of water, carboxylic acids, in particular C 2 -C 18 fatty acids such as acetic acid, stearic acid, aliphatic or aromatic alcohols, such as methanol, ethanol, isopropanol, phenolic antioxidants, primary or secondary amines such as antioxidants comprising the diaminophenylene unit. This variant of the process makes it possible to synthesize a copolymer comprising a monofunctional copolymer chain, since the copolymer chain A of the copolymer bears the function B1 at the end of the chain provided by step (a) of the process.
Selon une autre variante de l'invention, l'étape (b) est une réaction du composé de formule (II) avec un agent de fonctionnalisation. La réaction de fonctionnalisation fait intervenir la rupture de la liaison formée par Y et le carbone à la fois adjacent à Y et appartenant à la chaîne copolymère A. L'agent de fonctionnalisation est choisi par l'homme du métier pour sa réactivité vis-à-vis de cette liaison et pour la nature chimique de la fonction Z qu'il porte. L'étape (b) étant alors une réaction de fonctionnalisation, le procédé permet d'accéder selon cette autre variante à un copolymère téléchélique ou hétéro-téléchélique, puisqu'une extrémité de la chaîne copolymère A porte la fonction B1 apportée par l'étape (a), et l'autre extrémité la fonction Z apportée par l'étape (b).According to another variant of the invention, step (b) is a reaction of the compound of formula (II) with a functionalizing agent. The functionalization reaction involves the breaking of the bond formed by Y and the carbon both adjacent to Y and belonging to the copolymer chain A. The functionalization agent is chosen by the person skilled in the art for its reactivity vis-à-vis this bond and for the chemical nature of the Z function that it carries. Step (b) then being a functionalization reaction, the method allows access according to this other variant to a telechelic or hetero-telechelic copolymer, since one end of the copolymer chain A carries the B1 function provided by step (a), and the other end the Z function provided by step (b).
Généralement, la réaction de terminaison est conduite par la mise en contact du milieu réactionnel de polymérisation avec un agent de terminaison, qu'il soit stoppeur ou agent de de fonctionnalisation, à un taux de conversion des monomères choisi par l'homme du métier selon la macrostructure souhaitée du copolymère.Generally, the termination reaction is carried out by bringing the polymerization reaction medium into contact with a termination agent, whether it is a stopper or a functionalizing agent, at a monomer conversion rate chosen by the person skilled in the art according to the desired macrostructure of the copolymer.
L'étape (c) est une étape optionnelle selon que l'on souhaite ou non transformer la fonction B1, notamment en la fonction B2. Le mode de réalisation du procédé qui comprend l'étape (c) peut s'appliquer aux deux variantes du procédé décrites précédemment. Dans certains modes de réalisation très particuliers, l'étape (c) peut être conduite simultanément à l'étape (b). A titre d'exemple où l'étape (b) et (c) sont concomitantes, on peut citer le cas où l'étape (b) est une réaction de terminaison par un composé acide et l'étape (c) est une réaction de déprotection de la fonction B1 dans des conditions acides.Step (c) is an optional step depending on whether or not it is desired to transform function B1, in particular into function B2. The embodiment of the method which comprises step (c) can be applied to the two variants of the method described previously. In certain very particular embodiments, step (c) can be carried out simultaneously with step (b). By way of example where step (b) and (c) are concomitant, mention may be made of the case where step (b) is a termination reaction with an acid compound and step (c) is a deprotection reaction of the B1 function under acidic conditions.
Selon un mode de réalisation de l'invention particulier, l'étape (c) est une réaction de déprotection de la fonction B1 en B2, conduite en milieu acide ou basique selon la nature chimique de la fonction B1 à déprotéger. Par exemple, le groupe triméthylsilyle qui protège la fonction amine peut être hydrolysé en milieu acide ou basique. Le choix des conditions de déprotection est fait judicieusement par l'homme du métier en tenant compte de la structure chimique du substrat à déprotéger.According to a particular embodiment of the invention, step (c) is a reaction for deprotection of the function B1 in B2, carried out in an acidic or basic medium depending on the chemical nature of the function B1 to be deprotected. For example, the trimethylsilyl group which protects the amine function can be hydrolyzed in an acidic or basic medium. The choice of the conditions of deprotection is done judiciously by a person skilled in the art, taking into account the chemical structure of the substrate to be deprotected.
Le copolymère préparé selon le procédé conforme à l'invention peut être séparé du milieu réactionnel de l'étape (b) ou (c) selon des procédés bien connus de l'homme du métier, par exemple par une opération d'évaporation du solvant sous pression réduite ou par une opération de stripping à la vapeur d'eau.The copolymer prepared according to the process in accordance with the invention can be separated from the reaction medium of step (b) or (c) according to processes well known to those skilled in the art, for example by an operation of evaporation of the solvent under reduced pressure or by a steam stripping operation.
L'étape (a) du procédé conforme à l'invention requiert la préparation du composé de formule (II). Le composé de formule (II) est préparé par la copolymérisation d'un mélange monomère contenant le monomère M1 et le monomère M2 en la présence d'un système catalytique comprenant un agent de transfert de formule (III) et un catalyseur métallocène,
Y((CH2)dB1)y (III)
Step (a) of the process in accordance with the invention requires the preparation of the compound of formula (II). The compound of formula (II) is prepared by the copolymerization of a monomer mixture containing the monomer M1 and the monomer M2 in the presence of a catalytic system comprising a transfer agent of formula (III) and a metallocene catalyst,
Y((CH 2 ) d B1) y (III)
Y, B1, d et y étant tels que définis précédemment, en particulier dans les différents modes de réalisation décrits de l'invention.Y, B1, d and y being as defined previously, in particular in the various described embodiments of the invention.
La copolymérisation d'un mélange monomère contenant un diène conjugué et un monooléfine tel que l'éthylène, une α-monooléfines ou leur mélange peut être conduite conformément aux demandes de brevet
Par ailleurs, l'homme du métier adapte les conditions de polymérisation et les concentrations en chacun des réactifs (constituants du système catalytiques, monomères, stoppeur), selon le matériel (outils, réacteurs) utilisé pour conduire la polymérisation et les différentes réactions chimiques. Comme cela est connu de l'homme du métier, la copolymérisation ainsi que la manipulation des monomères, du système catalytique et du ou des solvants de polymérisation se font dans des conditions anhydres et sous atmosphère inerte. Les solvants de polymérisation sont typiquement des solvants hydrocarbonés, aliphatiques ou aromatiques.Furthermore, a person skilled in the art adapts the polymerization conditions and the concentrations of each of the reagents (constituents of the catalytic system, monomers, stopper), according to the equipment (tools, reactors) used to carry out the polymerization and the various chemical reactions. As is known to those skilled in the art, the copolymerization as well as the handling of the monomers, of the catalytic system and of the polymerization solvent(s) take place under anhydrous conditions and under an inert atmosphere. Polymerization solvents are typically hydrocarbon, aliphatic or aromatic solvents.
Le monomère M1 est de préférence un monomère choisi dans le groupe constitué par le 1,3-butadiène, l'isoprène et leur mélange, de manière plus préférentielle est le 1,3-butadiène. Le monomère M2 est l'éthylène ou un mélange d'éthylène et d'une α-monooléfine. A titre d'α-monooléfine conviennent celles citées précédemment, à savoir les α-monooléfines aliphatiques ou aromatiques, particulièrement les α-monooléfines aliphatiques ayant de préférence 3 à 18 atomes de carbone telles que le propène, le 1-butène, le 1-hexène, le 1-octène, le 1-hexadécène ou leurs mélanges.The monomer M1 is preferably a monomer chosen from the group consisting of 1,3-butadiene, isoprene and their mixture, more preferably is 1,3-butadiene. The monomer M2 is ethylene or a mixture of ethylene and an α-monoolefin. Suitable α-monoolefins are those mentioned above, namely aliphatic or aromatic α-monoolefins, particularly aliphatic α-monoolefins preferably having 3 to 18 carbon atoms such as propene, 1-butene, 1-hexene, 1-octene, 1-hexadecene or mixtures thereof.
L'agent de transfert est de préférence de formule (III-a) ou (III-b), avec d allant de 1 à 11, de préférence étant égal à 3. Le mode de réalisation dans lequel d est égal à 3 est avantageux notamment du point de vue de l'accessibilité de l'agent de transfert, puisque le réactif nécessaire à sa synthèse est un produit commercial ou un produit lui aussi facilement accessible par synthèse.
Mg[(CH2)d-N(SiMe2CH2CH2SiMe2)]2 (III-a)
Mg[(CH2)d-N(SiMe3)2]2 (III-b)
The transfer agent is preferably of formula (III-a) or (III-b), with d ranging from 1 to 11, preferably being equal to 3. The embodiment in which d is equal to 3 is advantageous in particular from the point of view of the accessibility of the transfer agent, since the reagent necessary for its synthesis is a commercial product or a product which is also easily accessible by synthesis.
Mg[(CH 2 ) d -N(SiMe 2 CH 2 CH 2 SiMe 2 )] 2 (III-a)
Mg[(CH 2 ) d -N(SiMe 3 ) 2 ] 2 (III-b)
Lorsque Y est un alcalino-terreux ou le zinc, l'agent de transfert peut être préparé par réaction de la forme métallique de Y, dit réactif, avec un substrat de formule X-(CH2)d-B1, B1 et d étant tel que définis précédemment, X étant un halogène, de préférence un atome de brome. Lorsque Y est Al, l'agent de transfert de formule (III) est préparé de préférence par réaction de AlCl3 avec un dérivé d'un composé de formule X-(CH2)d-B1 décrit ci-dessus, ce dérivé pouvant être un sel ionique à base de lithium ou de potassium, par exemple de formule respective Li(CH2)d-B1 ou K(CH2)d-B1 ou leur forme complexée avec un solvant, comme cela est bien connu dans les composés organométalliques à base de lithium ou de potassium.When Y is an alkaline earth metal or zinc, the transfer agent can be prepared by reaction of the metallic form of Y, called reactive, with a substrate of formula X-(CH 2 ) d -B1, B1 and d being as defined previously, X being a halogen, preferably a bromine atom. When Y is Al, the transfer agent of formula (III) is preferably prepared by reaction of AlCl 3 with a derivative of a compound of formula X-(CH 2 ) d -B1 described above, this derivative possibly being an ionic salt based on lithium or potassium, for example of the respective formula Li(CH 2 ) d -B1 or K(CH 2 ) d -B1 or their form complexed with a solvent, as is well known in organometallic compounds based on lithium or potassium.
L'agent de transfert est typiquement synthétisé dans des conditions opératoires généralement utilisées dans la synthèse des composés organométalliques, c'est-à-dire dans des conditions anhydres et sous atmosphère inerte, dans des solvants éthers, par un ajout contrôlé d'une solution du substrat, tel qu'un goutte à goutte, au réactif en suspension dans le solvant. La récupération de l'agent de transfert se fait de manière connue en soi, par exemple par évaporation du solvant de synthèse ou par recristallisation dans un solvant ou un mélange de solvants.The transfer agent is typically synthesized under operating conditions generally used in the synthesis of organometallic compounds, that is to say under anhydrous conditions and under an inert atmosphere, in ether solvents, by a controlled addition of a solution of the substrate, such as a drop by drop, to the reagent in suspension in the solvent. The transfer agent is recovered in a manner known per se, for example by evaporation of the synthesis solvent or by recrystallization from a solvent or a mixture of solvents.
Selon une première variante du procédé, le catalyseur métallocène est un métallocène comportant le motif (en anglais « moiety ») de formule (IV-1)
P(Cp1)(Cp2)Met (IV-1)
According to a first variant of the process, the metallocene catalyst is a metallocene comprising the unit (in English “moiety”) of formula (IV-1)
P(Cp 1 )(Cp 2 )Met (IV-1)
Met étant un atome de métal du groupe 4 ou un atome de métal de terre rare,
Cp1 et Cp2, identiques ou différents, étant choisis dans le groupe constitué par les groupes cyclopentadiényles, les groupes indényles et les groupes fluorényles, les groupes pouvant être substitués ou non,Met being a group 4 metal atom or a rare earth metal atom,
Cp 1 and Cp 2 , identical or different, being chosen from the group consisting of cyclopentadienyl groups, indenyl groups and fluorenyl groups, the groups possibly being substituted or not,
P étant un groupe pontant les deux groupes Cp1 et Cp2, et comprenant au moins un atome de silicium ou de carbone.P being a group bridging the two groups Cp 1 and Cp 2 , and comprising at least one atom silicon or carbon.
Dans la formule (IV-1), l'atome Met est relié à une molécule de ligand constituée des deux groupes Cp1 et Cp2 reliés entre eux par le pont P.In formula (IV-1), the Met atom is connected to a ligand molecule consisting of the two groups Cp 1 and Cp 2 linked together by the bridge P.
Selon une deuxième variante du procédé, le catalyseur métallocène est un métallocène comportant le motif (en anglais « moiety ») de formule (IV-2)
(Cp1)(Cp2)Met (IV-2)
According to a second variant of the process, the metallocene catalyst is a metallocene comprising the unit (in English “moiety”) of formula (IV-2)
(Cp 1 )(Cp 2 )Met (IV-2)
Met étant un atome de métal du groupe 4 ou un atome de métal de terre rare,
Cp1 et Cp2, identiques ou différents, étant choisis dans le groupe constitué par les groupes cyclopentadiényles, les groupes indényles et les groupes fluorényles, les groupes pouvant être substitués ou non.Met being a group 4 metal atom or a rare earth metal atom,
Cp 1 and Cp 2 , identical or different, being chosen from the group consisting of cyclopentadienyl groups, indenyl groups and fluorenyl groups, the groups possibly being substituted or not.
On rappelle que les terres rares sont des métaux et désignent les éléments scandium, yttrium et les lanthanides dont le numéro atomique varie de 57 à 71.It is recalled that the rare earths are metals and designate the elements scandium, yttrium and the lanthanides whose atomic number varies from 57 to 71.
A titre de groupes cyclopentadiényles, fluorényles et indényles substitués, on peut citer ceux substitués par des radicaux alkyles ayant 1 à 6 atomes de carbone ou par des radicaux aryles ayant 6 à 12 atomes de carbone. Le choix des radicaux est aussi orienté par l'accessibilité aux molécules correspondantes que sont les cyclopentadiènes, les fluorènes et indènes substitués, parce que ces derniers sont disponibles commercialement ou facilement synthétisables.As substituted cyclopentadienyl, fluorenyl and indenyl groups, mention may be made of those substituted by alkyl radicals having 1 to 6 carbon atoms or by aryl radicals having 6 to 12 carbon atoms. The choice of the radicals is also oriented by the accessibility to the corresponding molecules which are the substituted cyclopentadienes, fluorenes and indenes, because the latter are commercially available or easily synthesized.
Dans le cas d'un métallocène ponté de formule (IV-1), à titre de groupe cyclopentadiényle substitué, on peut citer particulièrement ceux substitués en position 2 ou 3, tels que les groupes tétraméthylcyclopentadiényle, 3-triméthylsilylcyclopentadiényle. La position 2 (ou 5) désigne la position de l'atome de carbone qui est adjacent à l'atome de carbone auquel est attaché le pont P, comme cela est représenté dans le schéma ci-après.
Dans le cas d'un métallocène ponté de formule (IV-1), à titre de groupe indényle substitué en position 2, on peut citer particulièrement ceux substitués en position 2 tels que les groupes 2-méthylindényle, 2-phénylindényle. La position 2 désigne la position de l'atome de carbone qui est adjacent à l'atome de carbone auquel est attaché le pont P, comme cela est représenté dans le schéma ci-après.
Dans le cas d'un métallocène ponté de formule (IV-1), à titre de groupes fluorényles substitués, on peut citer plus particulièrement les groupes 2,7-ditertiobutyle-fluorényle et 3,6-ditertiobutyle-fluorényle. Les positions 2, 3, 6 et 7 désignent respectivement la position des atomes de carbone des cycles comme cela est représenté dans le schéma ci-après, la position 9 correspondant à l'atome de carbone auquel est attaché le pont P.
Dans le cas d'un métallocène non ponté de formule (IV-2), à titre de groupe cyclopentadiényle substitué, on peut citer les groupes 3-triméthylsilylcyclopentadiényle, tétraméthylcyclopentadiényle ; à titre de groupe indényle substitué, on peut citer les groupes méthylindényle, phénylindényle ; à titre de groupes fluorényles substitués, on peut citer les groupes 2,7-ditertiobutyle-fluorényle et 3,6-ditertiobutyle-fluorényle.In the case of an unbridged metallocene of formula (IV-2), as substituted cyclopentadienyl group, mention may be made of 3-trimethylsilylcyclopentadienyl, tetramethylcyclopentadienyl; as a substituted indenyl group, mention may be made of methylindenyl and phenylindenyl groups; as substituted fluorenyl groups, mention may be made of the 2,7-ditertiobutyl-fluorenyl and 3,6-ditertiobutyl-fluorenyl groups.
Avantageusement, que le métallocène soit de formule (IV-1) ou (IV-2), Cp1 représente un groupe cyclopentadiényle substitué ou non substitué et Cp2 représente un groupe fluorényle substitué ou non substitué. Mieux, Cp1 représente un groupe cyclopentadiényle non substitué et Cp2 représente un groupe fluorényle non substitué.Advantageously, whether the metallocene is of formula (IV-1) or (IV-2), Cp 1 represents a substituted or unsubstituted cyclopentadienyl group and Cp 2 represents a substituted or unsubstituted fluorenyl group. More preferably, Cp 1 represents an unsubstituted cyclopentadienyl group and Cp 2 represents an unsubstituted fluorenyl group.
De préférence, le symbole P, désigné sous le terme de pont, répond à la formule MR1R2, M représentant un atome de silicium ou de carbone, de préférence un atome de silicium, R1 et R2, identiques ou différents, représentant un groupe alkyle comprenant de 1 à 20 atomes de carbone. De manière plus préférentielle, le pont P est de formule SiR1R2, R1 et R2, étant tels que définis précédemment. De manière encore plus préférentielle, il répond à la formule SiMe2.Preferably, the symbol P, designated by the term bridge, corresponds to the formula MR 1 R 2 , M representing a silicon or carbon atom, preferably a silicon atom, R 1 and R 2 , identical or different, representing an alkyl group comprising from 1 to 20 carbon atoms. More preferably, the bridge P has the formula SiR 1 R 2 , R 1 and R 2 , being as defined previously. Even more preferentially, it corresponds to the formula SiMe 2 .
Que le métallocène soit de formule (IV-1) ou (IV-2), le symbole Met représente de préférence un atome de métal de terre rare, de manière plus préférentielle un atome de lanthanide (Ln) dont le numéro atomique va de 57 à 71, de manière encore plus préférentielle un atome de néodyme (Nd).Whether the metallocene is of formula (IV-1) or (IV-2), the symbol Met preferably represents a rare earth metal atom, more preferably a lanthanide (Ln) atom whose atomic number ranges from 57 to 71, even more preferably a neodymium (Nd).
Selon un mode de réalisation préférentiel de l'invention, le catalyseur métallocène est de formule (IV-1a) ou (IV-2b)
{P(Cp1)(Cp2)Met-G}b (IV-1a)
{(Cp1)(Cp2)Met-G}b (IV-2b)
dans lesquelles
- Met représente un atome de métal de terre rare,
- le symbole G désignant un halogène X choisi dans le groupe constitué par le chlore, le fluor, le brome et l'iode, ou un groupe comprenant le motif borohydrure BH4,
- P, Cp1 et Cp2 étant tels que définis précédemment,
- b étant égal à 1 ou 2.
{P(Cp 1 )(Cp 2 )Met-G} b (IV-1a)
{(Cp 1 )(Cp 2 )Met-G} b (IV-2b)
in which
- Met represents a rare earth metal atom,
- the symbol G designating a halogen X chosen from the group consisting of chlorine, fluorine, bromine and iodine, or a group comprising the borohydride unit BH 4 ,
- P, Cp 1 and Cp 2 being as defined previously,
- b being equal to 1 or 2.
Que le métallocène soit de formule (IV-1a) ou (IV-2b), le symbole Met représente de préférence un atome de lanthanide (Ln) dont le numéro atomique va de 57 à 71, de manière plus préférentielle un atome de néodyme (Nd).Whether the metallocene is of formula (IV-1a) or (IV-2b), the symbol Met preferably represents a lanthanide (Ln) atom whose atomic number ranges from 57 to 71, more preferably a neodymium atom (Nd).
Le métallocène peut se trouver sous la forme de poudre cristallisée on non, ou encore sous la forme de monocristaux. Le métallocène peut se présenter sous une forme monomère ou dimère, ces formes dépendant du mode de préparation du métallocène, comme par exemple cela est décrit dans les demandes
Avantageusement, que le métallocène soit de formule (IV-1a) ou (IV-2b), Cp1 représente un groupe cyclopentadiényle substitué ou non substitué et Cp2 représente un groupe fluorényle substitué ou non substitué. Mieux, Cp1 représente un groupe cyclopentadiényle non substitué et Cp2 représente un groupe fluorényle non substitué. Le groupe fluorényle non substitué est de formule C13H8.Advantageously, whether the metallocene is of formula (IV-1a) or (IV-2b), Cp 1 represents a substituted or unsubstituted cyclopentadienyl group and Cp 2 represents a substituted or unsubstituted fluorenyl group. More preferably, Cp 1 represents an unsubstituted cyclopentadienyl group and Cp 2 represents an unsubstituted fluorenyl group. The unsubstituted fluorenyl group has the formula C 13 H 8 .
Selon l'un quelconque des modes de réalisation décrits, le catalyseur métallocène est de préférence un métallocène borohydrure de lanthanide ou un métallocène halogénure de lanthanide, notamment un métallocène chlorure de lanthanide.According to any one of the embodiments described, the metallocene catalyst is preferably a lanthanide borohydride metallocene or a lanthanide halide metallocene, in particular a lanthanide chloride metallocene.
Selon un mode de réalisation particulièrement préférentiel de l'invention, le symbole G désigne le chlore ou le groupe de formule (IV)
(BH4)(1+c)-Lc-Nx (IV)
dans laquelle
- L représente un métal alcalin choisi dans le groupe constitué par le lithium, le sodium et le potassium
- N représente une molécule d'un éther,
- x, nombre entier ou non, est égal ou supérieur à 0,
- c, nombre entier, est égal ou supérieur à 0.
(BH 4 ) (1+c)- L c -N x (IV)
in which
- L represents an alkali metal selected from the group consisting of lithium, sodium and potassium
- N represents a molecule of an ether,
- x, whole number or not, is equal to or greater than 0,
- c, whole number, is equal to or greater than 0.
Comme éther convient tout éther qui a le pouvoir de complexer le métal alcalin, notamment le diéthyléther et le tétrahydrofuranne.Suitable ether is any ether which has the power to complex the alkali metal, in particular diethyl ether and tetrahydrofuran.
De manière plus préférentielle, le catalyseur métallocène est de formule (IV-3a) ou (IV-3b) ou (IV-3c).
[Me2Si(C5H4)(C13H8)NdCl] (IV-3a)
[Me2Si(C5H4)(C13H8)Nd(BH4)2Li(THF)] (IV-3b)
[Me2Si(C5H4)(C13H8)Nd(BH4)(THF)] (IV-3c)
More preferably, the metallocene catalyst is of formula (IV-3a) or (IV-3b) or (IV-3c).
[Me 2 Si(C 5 H 4 )(C 13 H 8 )NdCl] (IV-3a)
[Me 2 Si(C 5 H 4 )(C 13 H 8 )Nd(BH 4 ) 2 Li(THF)] (IV-3b)
[Me 2 Si(C 5 H 4 )(C 13 H 8 )Nd(BH 4 )(THF)] (IV-3c)
Ainsi, l'utilisation de l'agent de transfert, autre objet de l'invention, permet d'accéder aux copolymères conformes à l'invention, qu'ils soient monofonctionnels en extrémité de chaîne ou téléchéliques. De tels copolymères répondent en particulier aux formules suivantes (V) et (VI)
H-A-(CH2)d-B (V)
Z-A-(CH2)d-B (VI)
- H représentant un atome d'hydrogène ;
- A représentant la chaîne copolymère telle que définie précédemment selon l'un quelconque des modes de réalisation de l'invention ;
- B et d étant tels que définis précédemment selon l'un quelconque des modes de réalisation de l'invention.
HA-( CH2 ) d -B(V)
ZA-( CH2 ) d -B(VI)
- H representing a hydrogen atom;
- A representing the copolymer chain as defined previously according to any one of the embodiments of the invention;
- B and d being as defined previously according to any one of the embodiments of the invention.
Un objet décrit par la présente est le composé de formule (II), dont la préparation est requise dans l'étape (a) du procédé conforme à l'invention,
Y(A-(CH2)d-B1)y (II)
- y étant égal à 2 ou 3,
- lorsque y = 2, le symbole Y étant un alcalino-terreux ou le zinc, et lorsque y = 3, Y étant l'aluminium ;
- d étant un nombre entier de 0 à 50, avantageusement de 0 à 11 ;
- le symbole A représentant la chaîne copolymère A définie selon l'un quelconque des modes de réalisation décrits,
- B1 étant choisi dans le groupe constitué par N(SiMe3)2; N(SiMe2CH2CH2SiMe2); para-C6H4(NMe2); para-C6H4(OMe); para-C6H4(N(SiMe3)2); ortho-CH2-C6H4NMe2; ortho-CH2-C6H4OMe; C6F5; C3F7; C6F13; CH(OCH2CH2O).
Y(A-(CH 2 ) d -B1) y (II)
- y being equal to 2 or 3,
- when y = 2, the symbol Y being an alkaline earth or zinc, and when y = 3, Y being aluminum;
- d being an integer from 0 to 50, advantageously from 0 to 11;
- the symbol A representing the copolymer chain A defined according to any one of the embodiments described,
- B1 being chosen from the group consisting of N(SiMe 3 ) 2 ; N(SiMe 2 CH 2 CH 2 SiMe 2 ); para-C 6 H 4 (NMe 2 ); para-C 6 H 4 (OMe); para-C 6 H 4 (N(SiMe 3 ) 2 ); ortho-CH 2 -C 6 H 4 NMe 2 ; ortho-CH 2 -C 6 H 4 OMe; C6F5 ; C3F7 ; C6F13 ; CH(OCH 2 CH 2 O).
Plus particulièrement, le composé de formule (II) est tel que Y est Mg, B1 représente le groupe N(SiMe2CH2CH2SiMe2) ou le groupe N(SiMe3)2 et d va de 1 à 11 ou égal à 3.More particularly, the compound of formula (II) is such that Y is Mg, B1 represents the N(SiMe 2 CH 2 CH 2 SiMe 2 ) group or the N(SiMe 3 ) 2 group and d ranges from 1 to 11 or equal to 3.
Le copolymère conforme à l'invention, notamment lorsqu'il est un élastomère, peut être utilisé dans une composition de caoutchouc, en particulier dans un produit semi-fini pour pneumatique.The copolymer in accordance with the invention, in particular when it is an elastomer, can be used in a rubber composition, in particular in a semi-finished product for a tire.
La composition de caoutchouc conforme à l'invention peut contenir en plus du copolymère tout ingrédient traditionnellement utilisé dans une composition de caoutchouc pour pneumatique, comme par exemple une charge renforçante telle qu'un noir de carbone ou une silice, un système plastifiant, un système de réticulation, en particulier de vulcanisation, un ou des antioxydants.The rubber composition in accordance with the invention may contain, in addition to the copolymer, any ingredient traditionally used in a rubber composition for tires, such as for example a reinforcing filler such as a carbon black or a silica, a plasticizing system, a crosslinking system, in particular vulcanization, one or more antioxidants.
Les caractéristiques précitées de la présente invention, ainsi que d'autres, seront mieux comprises à la lecture de la description suivante de plusieurs exemples de réalisation de l'invention, donnés à titre illustratif et non limitatif.The aforementioned features of the present invention, as well as others, will be better understood on reading the following description of several embodiments of the invention, given by way of non-limiting illustration.
Les analyses de SEC ont été réalisées à haute température (HT-SEC) en utilisant un appareil Viscotek (de Malvern Instruments) équipé avec 3 colonnes (PLgel Olexis 300 mm x 7 mm I. D. de Agilent Technologies) et de 3 détecteurs (réfractomètre, viscosimètre et diffusion de la lumière). 200 µL d'une solution de l'échantillon à une concentration de 5 mg mL-1 ont été élués dans le 1,2,4-trichlorobenzene en utilisant un débit de 1 mL min-1 à 150°C. La phase mobile a été stabilisée par du 2,6-di(tert-butyl)-4-methylphénol (200 mg L-1). Le logiciel OmniSEC a été utilisé pour l'acquisition et l'analyse des données. Les masses molaires moyennes en nombre Mn et l'indice de polydispersité Ð ont été calculées par calibration universelle en utilisant des standards de polystyrène.The SEC analyzes were carried out at high temperature (HT-SEC) using a Viscotek apparatus (from Malvern Instruments) equipped with 3 columns (PLgel Olexis 300 mm x 7 mm ID from Agilent Technologies) and 3 detectors (refractometer, viscometer and light scattering). 200 µL of a sample solution at a concentration of 5 mg mL -1 was eluted in 1,2,4-trichlorobenzene using a flow rate of 1 mL min -1 at 150°C. The mobile phase was stabilized with 2,6-di(tert-butyl)-4-methylphenol (200 mg L -1 ). OmniSEC software was used for data acquisition and analysis. The number-average molar masses Mn and the polydispersity index Ð were calculated by universal calibration using polystyrene standards.
La spectroscopie RMN haute résolution a été effectuée sur un spectromètre Bruker DRX 400 opérant à 400 MHz pour le proton et 101 MHz pour le carbone 13. Les acquisitions ont été faites à 363 K en utilisant une sonde 5 mm QNP pour le 1H et une sonde PSEX 10 mm pour le 13C NMR. Les échantillons ont été analysés à une concentration de 5-15 % en masse. Un mélange de tétrachloroéthylène (TCE) et de benzène deutéré (C6D6) (2/1 v/v) a été utilisé comme solvant. Les déplacements chimiques sont donnés en unité ppm, relativement au tétraméthylsilane comme référence interne pour la RMN 1H et au signal de méthylène à 30 ppm des enchaînement d'unités éthylène pour le 13C.High-resolution NMR spectroscopy was performed on a Bruker DRX 400 spectrometer operating at 400 MHz for the proton and 101 MHz for the carbon-13. The acquisitions were made at 363 K using a 5 mm QNP probe for the 1 H and a 10 mm PSEX probe for the 13 C NMR. The samples were analyzed at a concentration of 5-15% by mass. A mixture of tetrachlorethylene (TCE) and deuterated benzene (C6D6) (2/1 v/v) was used as solvent. The chemical shifts are given in units ppm, relative to tetramethylsilane as an internal reference for 1H NMR and to the methylene signal at 30 ppm of the sequence of ethylene units for 13 C.
La microstructure des copolymères éthylène/butadiène est déterminée par RMN 13C suivant la méthode décrite dans
Dans un ballon de 100 mL, on introduit sous atmosphère inerte d'argon, 2,6 g (2 équivalents) de magnésium puis 50 mL de THF sec.2.6 g (2 equivalents) of magnesium and then 50 mL of dry THF are introduced into a 100 mL flask under an inert argon atmosphere.
On additionne ensuite à température ambiante et goutte à goutte 13,3 mL (15 g, 1 équivalent) de 1-(3-bromopropyl)-2,2,5,5-tétraméthyl-1-aza-2,5-disilacyclopentane.13.3 mL (15 g, 1 equivalent) of 1-(3-bromopropyl)-2,2,5,5-tetramethyl-1-aza-2,5-disilacyclopentane are then added dropwise at room temperature.
On récupère ensuite la solution de 1-(3-bromopropyl)-2,2,5,5-tétraméthyl-1-aza-2,5-disilacyclopentane magnésium en canulant cette solution dans un tube de Schlenk sous argon afin d'éliminer le magnésium qui n'a pas réagi.The 1-(3-bromopropyl)-2,2,5,5-tetramethyl-1-aza-2,5-disilacyclopentane magnesium solution is then recovered by cannulating this solution into a Schlenk tube under argon in order to remove the unreacted magnesium.
On ajoute sur cette solution, 5,5 mL (1,2 équivalent) de dioxane afin de déplacer l'équilibre de Schlenk pour former le composé MgR2 (R= 1-propyl-2,2,5,5-tétramethyl-1-aza-2,5-disilacyclopentane) et précipiter MgBr2.5.5 mL (1.2 equivalent) of dioxane are added to this solution in order to shift the Schlenk equilibrium to form the compound MgR 2 (R=1-propyl-2,2,5,5-tetramethyl-1-aza-2,5-disilacyclopentane) and to precipitate MgBr 2 .
Cette solution est ensuite filtrée sous argon sur célite afin de récupérer MgR2 en solution dans le THF. On ajoute 100 mL de BuzO à cette solution et le THF est distillé sous vide à température ambiante.This solution is then filtered under argon on Celite in order to recover MgR 2 in solution in THF. 100 mL of BuzO are added to this solution and the THF is distilled under vacuum at room temperature.
On obtient ainsi une solution de MgR2 dans le Bu2O.A solution of MgR 2 in Bu 2 O is thus obtained.
Dans un ballon contenant 200 mL de toluène sec, on introduit 8,5 mL (1,96 mmol) de MgR2 (0,23 M dans le dibutyl éther) préparé suivant l'exemple 1.8.5 mL (1.96 mmol) of MgR 2 (0.23 M in dibutyl ether) prepared according to Example 1 are introduced into a flask containing 200 mL of dry toluene.
La solution est transférée sous atmosphère d'argon dans un réacteur de 250 mL.The solution is transferred under an argon atmosphere into a 250 mL reactor.
On transfère ensuite une solution de 31,3 mg de complexe [Me2SiFlu2Nd(BH4)2Li(THF)] (Nd = 49 µmol ; Mg/Nd = 40).A solution of 31.3 mg of complex [Me 2 SiFlu 2 Nd(BH 4 ) 2 Li(THF)] (Nd = 49 µmol; Mg/Nd = 40).
L'argon est éliminé sous vide et le réacteur est pressurisé à 4 bars au moyen d'un mélange gazeux de monomère éthylène / 1,3-butadiène de composition constante (5 % molaire de 1,3-butadiène) à 70°C.The argon is removed under vacuum and the reactor is pressurized to 4 bars using a gaseous mixture of ethylene/1,3-butadiene monomer of constant composition (5 molar % of 1,3-butadiene) at 70°C.
Le réacteur est dégazé au bout de 2 h de polymérisation et la température est ramenée à 20°C. Le milieu de polymérisation est versé dans une solution de méthanol/HCl 1M et est agité pendant 1 heure.The reactor is degassed after 2 h of polymerization and the temperature is brought back to 20°C. The polymerization medium is poured into a 1M methanol/HCl solution and is stirred for 1 hour.
Le polymère précipité est solubilisé dans le toluène puis est précipité dans une solution méthanol pour être ainsi lavé. Le polymère est finalement séché.The precipitated polymer is solubilized in toluene and then is precipitated in a methanol solution in order to be washed in this way. The polymer is finally dried.
On récupère 23,6 g de copolymère portant en extrémité de la chaîne copolymère la fonction NH3Cl attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-.23.6 g of copolymer carrying at the end of the copolymer chain the NH 3 Cl function attached to the chain via the —(CH 2 ) 3 — group are recovered.
La masse molaire moyenne en nombre est déterminée par analyse HT-SEC, 150°C : M n = 9 085 g mol-1, Ð = 2,18.The number-average molar mass is determined by HT-SEC analysis, 150° C.: M n =9085 g mol -1 , Ð = 2.18.
Le spectre de RMN proton (2/1 v/vTCE/CeDe, 400 MHz, 363K) montre le signal caractéristique du méthylène en position α de l'ammonium à δ = 2,68 ppm (large, -CH2-NH3Cl) et celui caractéristique des protons de l'ammonium à δ = 8,59 ppm (large, -NH 3Cl).The proton NMR spectrum (2/1 v/vTCE/CeDe, 400 MHz, 363K) shows the signal characteristic of methylene in the α position of ammonium at δ = 2.68 ppm (broad, -CH 2 -NH 3 Cl) and that characteristic of the protons of ammonium at δ = 8.59 ppm (broad, -NH 3 Cl).
La composition du copolymère est de 95,6 %mol d'éthylène. Le 1,3-butadiène est inséré à 24,7 %mol 1,4-trans, 11,0 %mol 1,2 et 64,3 %mol sous la forme de cycles.The composition of the copolymer is 95.6% mol of ethylene. 1,3-Butadiene is inserted at 24.7 mol% 1,4-trans, 11.0 mol% 1,2 and 64.3 mol% as rings.
Le même mode opératoire que l'exemple 2 est suivi pour la synthèse de ce copolymère mais avec un mélange de monomère à 20 %mol de 1,3-butadiène.The same procedure as Example 2 is followed for the synthesis of this copolymer but with a monomer mixture containing 20 mol% of 1,3-butadiene.
On récupère 7,3 g de copolymère portant en extrémité de la chaîne copolymère la fonction NH3Cl attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-.7.3 g of copolymer carrying at the end of the copolymer chain the NH 3 Cl function attached to the chain via the —(CH 2 ) 3 — group are recovered.
La masse molaire moyenne en nombre est déterminée par analyse HT-SEC , 150 °C : M n = 6 800 g mol-1, Ð = 2,07.The number-average molar mass is determined by HT-SEC analysis, 150° C.: M n =6,800 g mol -1 , Ð = 2.07.
Le spectre de RMN proton (2/1 v/vTCE/CeDe, 400 MHz, 363K) montre le signal caractéristique du méthylène en position α de l'ammonium à δ = 2,68 ppm (large, -CH 2-NH3 CI) et celui caractéristique des protons de l'ammonium à δ = 8,62 ppm (large, -NH 3Cl).The proton NMR spectrum (2/1 v/vTCE/CeDe, 400 MHz, 363K) shows the signal characteristic of methylene in the α position of ammonium at δ = 2.68 ppm (broad, -CH 2 -NH 3 CI) and that characteristic of the protons of ammonium at δ = 8.62 ppm (broad, -NH 3 Cl).
La composition du copolymère est de 80,0 %mol d'éthylène. Le 1,3-butadiène est inséré à 19,0 %mol 1,4-trans, 44,5 %mol 1,2 et 36,5 %mol sous la forme de cycles.The composition of the copolymer is 80.0 mol% ethylene. 1,3-Butadiene is inserted at 19.0 mol% 1,4-trans, 44.5 mol% 1,2 and 36.5 mol% as rings.
Le même mode opératoire que l'exemple 2 est suivi pour la synthèse de ce copolymère mais on introduit 2,2 mL (0,51 mmol) de MgR2 (0,23 M dans le dibutyl éther) pour 31,3 mg de complexe [Me2SiFlu2Nd(BH4)2Li(THF)] (Nd = 49 µmol ; Mg/Nd = 10,3) et on utilise un mélange de monomère à 20 %mol de 1,3-butadiène.The same procedure as Example 2 is followed for the synthesis of this copolymer, but 2.2 mL (0.51 mmol) of MgR 2 (0.23 M in dibutyl ether) is introduced for 31.3 mg of complex [Me 2 SiFlu 2 Nd(BH 4 ) 2 Li(THF)] (Nd=49 μmol; Mg/Nd=10.3) and a mixture of monomer at 20 %mol of 1,3-butadiene.
On récupère 16,8 g de copolymère portant en extrémité de la chaîne copolymère la fonction NH3Cl attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-.16.8 g of copolymer carrying at the end of the copolymer chain the NH 3 Cl function attached to the chain via the —(CH 2 ) 3 — group are recovered.
La masse molaire moyenne en nombre est déterminée par analyse HT-SEC, 150 °C : M n = 25 220 g mol-1, Ð = 2,2.The number-average molar mass is determined by HT-SEC analysis, 150° C.: M n =25,220 g mol -1 , Ð = 2.2.
Le spectre de RMN proton (2/1 v/vTCE/C6D6, 400 MHz, 363K) montre le signal caractéristique du méthylène en position α de l'ammonium à δ = 2,68 ppm (large, -CH 2-NH3 Cl) et celui caractéristique des protons de l'ammonium à δ = 8,62 ppm (large, -NH 3Cl).The proton NMR spectrum (2/1 v/vTCE/C 6 D 6 , 400 MHz, 363K) shows the characteristic signal of methylene in the α position of ammonium at δ = 2.68 ppm (broad, -C H 2 -NH 3 Cl) and that characteristic of the protons of ammonium at δ = 8.62 ppm (broad, -N H 3 Cl).
La composition du copolymère est de 80,1 %mol d'éthylène. Le 1,3-butadiène est inséré à 17,5 %mol 1,4-trans, 45,2 %mol 1,2 et 37,3 %mol sous la forme de cycles.The composition of the copolymer is 80.1% mol of ethylene. The 1,3-butadiene is inserted at 17.5 mol% 1,4- trans, 45.2 mol% 1,2 and 37.3 mol% in the form of rings.
Le même mode opératoire que l'exemple 4 est suivi pour la synthèse de ce copolymère mais la polymérisation dure cette fois 4 h.The same procedure as Example 4 is followed for the synthesis of this copolymer, but the polymerization this time lasts 4 hours.
On récupère 27,6 g de copolymère portant en extrémité de la chaîne copolymère la fonction NH3Cl attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-.27.6 g of copolymer carrying at the end of the copolymer chain the NH 3 Cl function attached to the chain via the —(CH 2 ) 3 — group are recovered.
La masse molaire moyenne en nombre est déterminée par analyse HT-SEC, 150 °C : M n = 39 730 g mol-1, Ð = 2,3.The number-average molar mass is determined by HT-SEC analysis, 150° C.: M n =39,730 g mol -1 , Ð = 2.3.
Le spectre de RMN proton (2/1 v/v TCE/C6D6, 400 MHz, 363K) permet d'observer le méthylène en position α de l'ammonium à δ = 2,68 ppm (large, -CH 2-NH3Cl).The proton NMR spectrum (2/1 v/v TCE/C 6 D 6 , 400 MHz, 363K) makes it possible to observe the methylene in the α position of the ammonium at δ=2.68 ppm (broad, -C H 2 -NH 3 Cl).
La composition du copolymère est de 79,3 %mol d'éthylène. Le 1,3-butadiène est inséré à 28,1 %mol 1,4-trans, 38,7 %mol 1,2 et 33,2 %mol sous la forme de cycles.The composition of the copolymer is 79.3% mol of ethylene. The 1,3-butadiene is inserted at 28.1% mol 1,4- trans, 38.7% mol 1,2 and 33.2% mol in the form of rings.
Le même mode opératoire que l'exemple 2 est suivi pour la synthèse de ce copolymère mais avec un mélange de monomère à 30 %mol de 1,3-butadiène.The same procedure as example 2 is followed for the synthesis of this copolymer but with a monomer mixture containing 30 mol% of 1,3-butadiene.
On récupère 7,3 g de copolymère portant en extrémité de la chaîne copolymère la fonction NH3Cl attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-.7.3 g of copolymer carrying at the end of the copolymer chain the NH 3 Cl function attached to the chain via the —(CH 2 ) 3 — group are recovered.
Le spectre de RMN proton (2/1 v/vTCE/C6D6, 400 MHz, 363K) montre le signal caractéristique du méthylène en position α de l'ammonium à δ = 2,68 ppm (large, -CH 2-NH3Cl) et celui caractéristique des protons de l'ammonium à δ = 8,59 ppm (large, -NH 3Cl).The proton NMR spectrum (2/1 v/vTCE/C 6 D 6 , 400 MHz, 363K) shows the characteristic signal of methylene in the α position of ammonium at δ = 2.68 ppm (broad, -C H 2 -NH 3 Cl) and that characteristic of the protons of ammonium at δ = 8.59 ppm (broad, -N H 3 Cl).
La composition du copolymère est de 75.3 %mol d'éthylène. Le 1,3-butadiène est inséré à 25,7 %mol 1,4-trans, 44,2 %mol 1,2 et 30.1 %mol sous la forme de cycles.The composition of the copolymer is 75.3% mol of ethylene. The 1,3-butadiene is inserted at 25.7% mol 1,4-trans, 44.2% mol 1,2 and 30.1% mol in the form of rings.
Dans un ballon contenant 200 mL de toluène sec, on introduit 1,24 mL (284 µmol) de MgR2 (0,23 M dans le dibutyl éther) préparé suivant l'exemple 1. La solution est transférée sous atmosphère d'argon dans un réacteur de 250 mL. On transfère ensuite une solution contenant 30,7 mg de complexe [Me2Si(C5H4)(C13H8)Nd(BH4)2Li(THF)] (Nd =57 µmol ; Mg/Nd = 5). L'argon est éliminé sous vide et le réacteur est pressurisé à 4 bars au moyen d'un mélange gazeux de monomère éthylène / 1,3-butadiène de composition constante (20 % molaire de 1,3-butadiène) à 80°C. Le réacteur est dégazé au bout de 90 minutes de polymérisation et la température est ramenée à 20°C. Le milieu de polymérisation est versé dans une solution de méthanol/HCl 1M et est agité pendant 1 heure. Le polymère précipité est re-solubilisé dans le toluène, puis est précipité dans une solution méthanol pour être ainsi lavé. Le polymère est finalement séché.1.24 mL (284 μmol) of MgR 2 (0.23 M in dibutyl ether) prepared according to Example 1 is introduced into a flask containing 200 mL of dry toluene. The solution is transferred under an argon atmosphere into a 250 mL reactor. A solution containing 30.7 mg of complex [Me 2 Si(C 5 H 4 )(C 13 H 8 )Nd(BH 4 ) 2 Li(THF)] (Nd=57 μmol; Mg/Nd=5) is then transferred. The argon is removed under vacuum and the reactor is pressurized to 4 bars by means of a gaseous mixture of ethylene/1,3-butadiene monomer of constant composition (20 molar % of 1,3-butadiene) at 80°C. The reactor is degassed after 90 minutes of polymerization and the temperature is brought back to 20°C. The polymerization medium is poured into a 1M methanol/HCl solution and is stirred for 1 hour. The precipitated polymer is re-solubilized in toluene, then is precipitated in a methanol solution to be washed in this way. The polymer is finally dried.
On récupère 9,89 g de copolymère portant en extrémité de la chaîne une fonction -NH3Cl (ou sous forme -NH2) attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-. Le spectre de RMN proton (2/1 v/v TCE/C6D6, 400 MHz, 363K) montre le signal caractéristique du méthylène en position α de l'amine à δ = 2,53 ppm (large, -CH 2-NH2) et celui du méthylène en position α de l'ammonium à δ = 2,68 ppm (large, -CH 2-NH3Cl). La composition du copolymère est de 67,6 %mol d'éthylène et de 32,4% de butadiène. Le 1,3-butadiène est inséré sous deux formes, 97,4 %mol de motifs 1,4-trans et 2,6 %mol d'unités 1,2.9.89 g of copolymer carrying at the end of the chain a —NH 3 Cl function (or in the —NH 2 form) attached to the chain via the —(CH 2 ) 3 — group are recovered. The proton NMR spectrum (2/1 v/v TCE/C 6 D 6 , 400 MHz, 363K) shows the characteristic signal of methylene in the α position of the amine at δ = 2.53 ppm (broad, -C H 2 -NH 2 ) and that of methylene in the α position of the ammonium at δ = 2.68 ppm (broad, -C H 2 -NH 3 Cl). The composition of the copolymer is 67.6% mol of ethylene and 32.4% of butadiene. The 1,3-butadiene is inserted in two forms, 97.4 mol% 1,4-trans units and 2.6 mol% 1,2 units.
Une fraction du polymère de l'exemple 2 est prélevée (10 g). Le polymère est solubilisé dans le toluène puis est précipité à l'aide d'une solution méthanol/NaOH (1M) et est agité pendant 1 heure à température ambiante.A fraction of the polymer of Example 2 is taken (10 g). The polymer is dissolved in toluene and then precipitated using a methanol/NaOH (1M) solution and stirred for 1 hour at room temperature.
Le polymère est récupéré puis lavé au méthanol et séché sous vide à 60°C.The polymer is recovered and then washed with methanol and dried under vacuum at 60°C.
On récupère 8,2 g de copolymère portant en extrémité de la chaîne copolymère la fonction NH2 attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-.8.2 g of copolymer carrying at the end of the copolymer chain the NH 2 function attached to the chain via the —(CH 2 ) 3 — group are recovered.
Le spectre de RMN proton (2/1 v/v TCE/C6D6, 400 MHz, 363K) montre la disparition des signaux caractéristiques de l'ammonium à δ = 2,68 ppm, (large, -CH 2-NH3Cl) et δ = 8,59 ppm, (large, -NH 3Cl) au profit du signal caractéristique du méthylène en position α de l'amine à δ = 2,53 ppm (large, -CH 2-NH2).The proton NMR spectrum (2/1 v/v TCE/C 6 D 6 , 400 MHz, 363K) shows the disappearance of the characteristic signals of ammonium at δ = 2.68 ppm, (broad, -C H 2 -NH 3 Cl) and δ = 8.59 ppm, (broad, -N H 3 Cl) in favor of the characteristic signal of methylene in the α position of the amine at δ = 2.5 3 ppm (broad, -CH 2 -NH 2 ).
Une fraction du polymère de l'exemple 3 est prélevée (8 g). Le polymère est solubilisé dans le toluène puis est précipité à l'aide d'une solution méthanol/NaOH (1M) et est agité pendant 1 heure à température ambiante.A fraction of the polymer of Example 3 is taken (8 g). The polymer is dissolved in toluene and then precipitated using a methanol/NaOH (1M) solution and stirred for 1 hour at room temperature.
Le polymère est récupéré puis lavé au méthanol et séché sous vide à 60°C.The polymer is recovered and then washed with methanol and dried under vacuum at 60°C.
On récupère 7,8 g de copolymère portant en extrémité de la chaîne copolymère la fonction NH2 attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-.7.8 g of copolymer carrying at the end of the copolymer chain the NH 2 function attached to the chain via the —(CH 2 ) 3 — group are recovered.
Le spectre de RMN proton (2/1 v/v TCE/C6D6, 400 MHz, 363K) montre la disparition des signaux caractéristiques de l'ammonium à δ = 2,68 ppm, (large, -CH 2-NH3Cl) et δ = 8,62 ppm, (large, -NH 3Cl) au profit du signal caractéristique du méthylène en position α de l'amine à δ = 2,53 ppm (large, -CH 2-NH2).The proton NMR spectrum (2/1 v/v TCE/C 6 D 6 , 400 MHz, 363K) shows the disappearance of the characteristic signals of ammonium at δ = 2.68 ppm, (broad, -C H 2 -NH 3 Cl) and δ = 8.62 ppm, (broad, -N H 3 Cl) in favor of the characteristic signal of methylene in the α position of the amine at δ = 2.5 3 ppm (broad, -CH 2 -NH 2 ).
Une fraction du polymère de l'exemple 4 est prélevée (7 g). Le polymère est solubilisé dans le toluène puis est précipité à l'aide d'une solution méthanol/NaOH (1M) et est agité pendant 1 heure à température ambiante.A fraction of the polymer of Example 4 is taken (7 g). The polymer is dissolved in toluene and then precipitated using a methanol/NaOH (1M) solution and stirred for 1 hour at room temperature.
Le polymère est récupéré puis lavé au méthanol et séché sous vide à 60°C.The polymer is recovered and then washed with methanol and dried under vacuum at 60°C.
On récupère 5,3 g de copolymère portant en extrémité de la chaîne copolymère la fonction NH2 attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-.5.3 g of copolymer carrying at the end of the copolymer chain the function NH 2 attached to the chain through the -(CH 2 ) 3 - group.
Une fraction du polymère de l'exemple 5 est prélevée (13 g). Le polymère est solubilisé dans le toluène puis est précipité à l'aide d'une solution méthanol/NaOH (1M) et est agité pendant 1 heure à température ambiante.A fraction of the polymer of Example 5 is taken (13 g). The polymer is dissolved in toluene and then precipitated using a methanol/NaOH (1M) solution and stirred for 1 hour at room temperature.
Le polymère est récupéré puis lavé au méthanol et séché sous vide à 60°C.The polymer is recovered and then washed with methanol and dried under vacuum at 60°C.
On récupère 12,0 g de copolymère portant en extrémité de la chaîne copolymère la fonction NH2 attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-.12.0 g of copolymer carrying at the end of the copolymer chain the NH 2 function attached to the chain via the —(CH 2 ) 3 — group are recovered.
Le spectre de RMN proton (2/1 v/v TCE/C6D6, 400 MHz, 363K) montre la disparition du signal caractéristique de l'ammonium observé à δ = 2,68 ppm, (large, -CH 2-NH3Cl) au profit du signal caractéristique du méthylène en position α de l'amine à δ = 2,53 ppm (large, -CH 2-NH2).The proton NMR spectrum (2/1 v/v TCE/C 6 D 6 , 400 MHz, 363K) shows the disappearance of the characteristic signal of ammonium observed at δ = 2.68 ppm, (broad, -C H 2 -NH 3 Cl) in favor of the characteristic signal of methylene in the α position of the amine at δ = 2.53 ppm (broad, -C H 2 -NH 2 ).
Une fraction du polymère de l'exemple 6 est prélevée (3 g). Le polymère est solubilisé dans le toluène puis est précipité à l'aide d'une solution méthanol/NaOH (1M) et est agité pendant 1 heure à température ambiante.A fraction of the polymer of Example 6 is taken (3 g). The polymer is dissolved in toluene and then precipitated using a methanol/NaOH (1M) solution and stirred for 1 hour at room temperature.
Le polymère est récupéré puis lavé au méthanol et séché sous vide à 60°C.The polymer is recovered and then washed with methanol and dried under vacuum at 60°C.
On récupère 2,5 g de copolymère portant en extrémité de la chaîne copolymère la fonction NH2 attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-.2.5 g of copolymer carrying at the end of the copolymer chain the NH 2 function attached to the chain via the —(CH 2 ) 3 — group are recovered.
Le spectre de RMN proton (2/1 v/v TCE/C6D6, 400 MHz, 363K) montre la disparition des signaux caractéristiques de l'ammonium à δ = 2,68 ppm, (large, -CH 2-NH3Cl) et δ = 8,59 ppm, (large, -NH 3Cl) au profit du signal caractéristique du méthylène en position α de l'amine à δ = 2,53 ppm (large, -CH 2-NH2).The proton NMR spectrum (2/1 v/v TCE/C 6 D 6 , 400 MHz, 363K) shows the disappearance of the characteristic signals of ammonium at δ = 2.68 ppm, (broad, -C H 2 -NH 3 Cl) and δ = 8.59 ppm, (broad, -N H 3 Cl) in favor of the characteristic signal of methylene in the α position of the amine at δ = 2.5 3 ppm (broad, -CH 2 -NH 2 ).
Dans un ballon contenant 200 mL de toluène sec, on introduit 8,5 mL (1,96 mmol) de MgR2 (0,23 M dans le dibutyl éther) préparé suivant l'exemple 1.8.5 mL (1.96 mmol) of MgR 2 (0.23 M in dibutyl ether) prepared according to Example 1 are introduced into a flask containing 200 mL of dry toluene.
La solution est transférée sous atmosphère d'argon dans un réacteur de 250 mL.The solution is transferred under an argon atmosphere into a 250 mL reactor.
On transfère ensuite une solution de 31,3 mg de complexe [Me2SiFlu2Nd(BH4)2Li(THF)] (Nd = 49 µmol ; Mg/Nd = 40).A solution of 31.3 mg of complex [Me 2 SiFlu 2 Nd(BH 4 ) 2 Li(THF)] (Nd=49 μmol; Mg/Nd=40) is then transferred.
L'argon est éliminé sous vide et le réacteur est pressurisé à 4 bars au moyen d'un mélange gazeux de monomère éthylène / 1,3-butadiène de composition constante (20 %molaire de 1,3-butadiène) à 70°C.The argon is removed under vacuum and the reactor is pressurized to 4 bars by means of a gaseous mixture of ethylene/1,3-butadiene monomer of constant composition (20% molar of 1,3-butadiene) at 70°C.
Le réacteur est dégazé au bout de 2 h de polymérisation et la température du milieu réactionnel est maintenue à 70°C.The reactor is degassed after 2 h of polymerization and the temperature of the medium reaction is maintained at 70°C.
Afin d'avoir un copolymère de référence avant la réaction avec l'agent de fonctionnalisation, en l'espèce le copolymère monofonctionnel, un prélèvement de 100 mL du milieu réactionnel est alors effectué. Ce prélèvement est versé dans une solution méthanol/HCl 1M et est agité pendant 1 heure. Le polymère de référence précipité est solubilisé dans le toluène puis est précipité dans une solution méthanol pour être ainsi lavé.In order to have a reference copolymer before the reaction with the functionalizing agent, in this case the monofunctional copolymer, a sample of 100 mL of the reaction medium is then taken. This sample is poured into a 1M methanol/HCl solution and is stirred for 1 hour. The precipitated reference polymer is solubilized in toluene and then is precipitated in a methanol solution in order to be washed in this way.
Le polymère est finalement séché.The polymer is finally dried.
On récupère 7,4 g de copolymère portant en extrémité de la chaîne copolymère la fonction NH3Cl attachée à la chaîne par l'intermédiaire du groupe -(CH2)3-.7.4 g of copolymer carrying at the end of the copolymer chain the NH 3 Cl function attached to the chain via the —(CH 2 ) 3 — group are recovered.
Le spectre de RMN proton (2/1 v/v TCE/C6D6, 400 MHz, 363K) montre le signal caractéristique du méthylène en position α de l'ammonium à δ = 2,68 ppm (large, -CH 2-NH3Cl) et celui caractéristique des protons de l'ammonium à δ = 8,58 ppm (large, -NH 3Cl)
La composition du copolymère de référence est de 80,8 %mol d'éthylène. Le 1,3-butadiène est inséré à 18,7 %mol 1,4-trans, 39,9 %mol 1,2 et 41,4 %mol sous la forme de cycles.The proton NMR spectrum (2/1 v/v TCE/C 6 D 6 , 400 MHz, 363K) shows the signal characteristic of methylene in the α position of ammonium at δ = 2.68 ppm (broad, -C H 2 -NH 3 Cl) and that characteristic of the protons of ammonium at δ = 8.58 ppm (broad, -N H 3 Cl)
The composition of the reference copolymer is 80.8% mol of ethylene. The 1,3-butadiene is inserted at 18.7% mol 1,4- trans, 39.9% mol 1,2 and 41.4% mol in the form of rings.
Au milieu réactionnel, une solution de 3,8 g d'iode (15 mmol) dans le THF (rapport molaire l/Mg = 15) est ajoutée et le mélange est agité pendant 2 heures à 70°C.To the reaction medium, a solution of 3.8 g of iodine (15 mmol) in THF (1/Mg molar ratio=15) is added and the mixture is stirred for 2 hours at 70°C.
La température est ramenée à 20°C. Le milieu de polymérisation est versé dans une solution méthanol/HCl 1M et est agité pendant 1 heure.The temperature is brought back to 20°C. The polymerization medium is poured into a 1M methanol/HCl solution and is stirred for 1 hour.
Le polymère précipité est solubilisé dans le toluène puis est précipité dans une solution méthanol pour être ainsi lavé.The precipitated polymer is solubilized in toluene and then is precipitated in a methanol solution in order to be washed in this way.
Le polymère est finalement séché.The polymer is finally dried.
On récupère 6,3 g de copolymère portant à une extrémité de chaîne la fonction NH3Cl attachée à la chaîne par l'intermédiaire du groupe -(CH2)3- et à l'autre extrémité de chaîne la fonction I.6.3 g of copolymer are recovered bearing at one chain end the NH 3 Cl function attached to the chain via the —(CH 2 ) 3 — group and at the other chain end the I function.
Le spectre de RMN proton (2/1 v/vTCE/C6D6, 400 MHz, 363K) montre le signal caractéristique du méthylène en position α de l'ammonium à δ = 2,68 ppm (large, -CH 2-NH3Cl) et celui caractéristique des protons de l'ammonium à δ = 8,52 ppm (large, -NH 3Cl) mais aussi celui caractéristique de méthylènes en position α d'un groupe iodo à δ = 2,94 ppm (multiplet, -CH 2-I). The proton NMR spectrum (2/1 v/vTCE/C 6 D 6 , 400 MHz, 363K) shows the characteristic signal of methylene in the α position of ammonium at δ = 2.68 ppm (broad, -C H 2 -NH 3 Cl) and that characteristic of the protons of ammonium at δ = 8.52 ppm (broad, -N H 3 Cl) but also that characteristic of methylenes in the α position of an iodo group at δ=2.94 ppm (multiplet, -C H 2 -I).
Claims (14)
- Copolymer comprising a copolymer chain A bearing a function B selected from the group consisting of the functions B1 and B2,• the copolymer chain A being a copolymer chain comprising monomer units M1 and monomer units M2, M1 being a conjugated diene,• B1 being selected from the group consisting of N(SiMe3)2; N(SiMe2CH2CH2SiMe2); para-C6H4(NMe2); para-C6H4(OMe); para-C6H4(N(SiMe3)2); ortho-CH2-C6H4NMe2; ortho-CH2-C6H4OMe; C6F5; C3F7; C6F13; CH(OCH2CH2O);• B2 being a function that is derived from B1;the function B being borne at the end of the copolymer chain A;M2 being ethylene or a mixture of ethylene and an α-monoolefin.
- Copolymer according to Claim 1, wherein the function B is attached to the copolymer chain A directly by a covalent bond or via a divalent group of formula (I)
-(CH2)w- (I)
wherein w is an integer from 1 to 50, preferably w varies in a range extending from 1 to 11, more preferably is equal to 3. - Copolymer according to any one of Claims 1 to 2, wherein the function B1 is the N(SiMe2CH2CH2SiMe2) group or the N(SiMe3)2 group.
- Copolymer according to any one of Claims 1 to 3, wherein the function B2 is selected from the group consisting of amines, ammoniums and ketones.
- Copolymer according to any one of Claims 1 to 4, wherein the function B2 is an amine, preferably a primary amine.
- Copolymer according to any one of Claims 1 to 5, wherein the ethylene units represent more than 50 mol%, preferentially more than 65 mol% of the monomer units of the copolymer.
- Copolymer according to any one of Claims 1 to 6, wherein the monomer units M1 contain more than 80 mol% of a moiety resulting from a trans-1,4 insertion of M1 into the copolymer chain.
- Process for preparing a copolymer comprising a copolymer chain A according to claim 1, which process comprises step (a), step (b) and where appropriate step (c) below:• (a) preparation of a compound of formula (II)
Y(A-(CH2)d-B1)y (II)
whereino y is equal to 2 or 3;o when y = 2, the symbol Y is an alkaline-earth metal or zinc, and when y = 3, Y is aluminium;o d is an integer from 0 to 50, advantageously from 0 to 11;o the symbol A representing a copolymer chain A comprising monomer units M1 and monomer units M2, M1 being a conjugated diene;o B1 is selected from the group consisting of N(SiMe3)2; N(SiMe2CH2CH2SiMe2); para-C6H4(NMe2); para-C6H4(OMe); para-C6H4(N(SiMe3)2); ortho-CH2-C6H4NMe2; ortho-CH2-C6H4OMe; C6F5; C3F7; C6F13; CH(OCH2CH2O),• (b) a reaction for terminating the copolymer chain A,• (c) a reaction for modifying the function B1 into the function B2 defined according to claim 1, M2 being ethylene or a mixture of ethylene and an α-monoolefin,the compound of formula (II) being prepared by the copolymerization of a monomer mixture containing the monomer M1 and the monomer M2 in the presence of a catalytic system comprising a transfer agent of formula (III) and a metallocene catalyst comprising the moiety of formula (IV-1) or (IV-2)
Y((CH2)dB1)y (III)
P(Cp1)(Cp2)Met (IV-1)
(Cp1)(Cp2)Met (IV-2)
Met being a group 4 metal atom or a rare-earth metal atom,P being a group that bridges the two Cp1 and Cp2 groups, and that comprises at least one silicon or carbon atom,Cp1 and Cp2, which are identical or different, being selected from the group consisting of cyclopentadienyl groups, indenyl groups and fluorenyl groups, it being possible for the groups to be substituted or unsubstituted. - Process according to Claim 8, wherein the transfer agent is of formula (III-a) or (III-b), with d ranging from 1 to 11:
Mg[(CH2)d-N(SiMe2CH2CH2SiMe2)]2 (III-a)
Mg[(CH2)d-N(SiMe3)2]2 (III-b)
- Process according to Claim 9, wherein d is equal to 3.
- Process according to any one of Claims 8 to 10, wherein Met represents a rare-earth metal atom, preferably a lanthanide atom Ln, the atomic number of which ranges from 57 to 71, more preferentially a neodymium atom.
- Process according to any one of Claims 8 to 11, wherein the metallocene catalyst is of formula (IV-1a) or (IV-2b):
{P(Cp1)(Cp2)Met-G}b (IV-1a)
{(Cp1)(Cp2)Met-G}b (IV-2b)
- the symbol G denoting a halogen X selected from the group consisting of chlorine, fluorine, bromine and iodine or a group comprising the BH4 borohydride moiety,- P, Cp1 and Cp2 being as defined in Claim 8,- Met being as defined in Claim 11,- b being equal to 1 or 2. - Compound of formula (II) as defined in Claim 8, preferably with Y being Mg, B1 representing the N(SiMe2CH2CH2SiMe2) group or the N(SiMe3)2 group and d ranging from 1 to 11 or being equal to 3.
- Rubber composition that comprises a copolymer defined according to any one of Claims 1 to 7, the copolymer being an elastomer.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1562012A FR3044664B1 (en) | 2015-12-08 | 2015-12-08 | MONOFUNCTIONAL OR TELECHELIC COPOLYMER OF 1,3-DIENE AND ETHYLENE OR ALPHA-MONOOLEFIN. |
PCT/EP2016/080064 WO2017097829A1 (en) | 2015-12-08 | 2016-12-07 | Monofunctional or telechelic copolymer of 1,3-diene and ethylene or alpha-monoolefin |
Publications (2)
Publication Number | Publication Date |
---|---|
EP3387024A1 EP3387024A1 (en) | 2018-10-17 |
EP3387024B1 true EP3387024B1 (en) | 2023-07-26 |
Family
ID=55589970
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP16809754.1A Active EP3387024B1 (en) | 2015-12-08 | 2016-12-07 | Monofunctional or telechelic copolymer of 1,3-diene and ethylene or alpha-monoolefin |
Country Status (7)
Country | Link |
---|---|
US (1) | US10752713B2 (en) |
EP (1) | EP3387024B1 (en) |
JP (1) | JP6876700B2 (en) |
CN (1) | CN108699171B (en) |
FR (1) | FR3044664B1 (en) |
SA (1) | SA518391692B1 (en) |
WO (1) | WO2017097829A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR3136466A1 (en) * | 2022-06-09 | 2023-12-15 | Compagnie Generale Des Etablissements Michelin | Process for the synthesis of polyethylenes or copolymers of ethylene and 1,3-diene carrying a terminal ketone function. |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2799468B1 (en) | 1999-10-12 | 2006-04-28 | Michelin Soc Tech | CATALYTIC SYSTEM USABLE FOR THE COPOLYMERIZATION OF ETHYLENE AND A CONJUGATE DIENE, PROCESS FOR THE PREPARATION OF THIS CATALYTIC SYSTEM AND OF A COPOLYMER OF ETHYLENE AND A CONJUGATE DIENE |
WO2004035639A1 (en) * | 2002-10-16 | 2004-04-29 | Societe De Technologie Michelin | Ethylene/butadiene copolymers, catalytic system of producing same and production of said polymers |
FR2858817B1 (en) | 2003-08-13 | 2006-02-03 | Michelin Soc Tech | CATALYTIC SYSTEM FOR OBTAINING CONJUGATED (S) / MONO-OLEFINE (S) DIENE (S) COPOLYMERS AND COPOLYMERS |
US7265195B2 (en) * | 2004-06-02 | 2007-09-04 | Acushnet Company | Compositions for golf equipment |
FR2893028B1 (en) | 2005-11-09 | 2008-02-15 | Michelin Soc Tech | METALOCENE COMPLEX BOROHYDRIDE OF LANTHANIDE, INCORPORATING CATALYTIC SYSTEM, POLYMERIZATION METHOD USING THE SAME, AND ETHYLENE / BUTADIENE COPOLYMER OBTAINED BY THIS PROCESS |
FR2893029B1 (en) | 2005-11-09 | 2009-01-16 | Michelin Soc Tech | METALOCENE COMPLEX BOROHYDRIDE OF LANTHANIDE, INCORPORATING CATALYTIC SYSTEM, POLYMERIZATION METHOD USING THE SAME, AND ETHYLENE / BUTADIENE COPOLYMER OBTAINED BY THIS PROCESS |
JP5246733B2 (en) | 2007-03-30 | 2013-07-24 | 旭化成ケミカルズ株式会社 | Modified polymer excellent in affinity with inorganic filler, method for producing the same, and composition thereof |
FR2946047B1 (en) * | 2009-06-02 | 2011-07-29 | Michelin Soc Tech | NOVEL ORGANOMETALLIC COMPOUNDS BASED ON A METAL BELONGING TO THE 2ND COLUMN OF PERIODIC CLASSIFICATION AND PROCESS FOR PREPARING THE SAME |
FR2946048B1 (en) * | 2009-06-02 | 2012-12-28 | Michelin Soc Tech | CATALYTIC SYSTEM FOR POLYMERIZATION OF CONJUGATED DIENES, POLYMERISATION METHOD AND FUNCTIONAL POLYMER OBTAINED |
CA2768987A1 (en) * | 2009-07-29 | 2011-02-03 | Dow Global Technologies Llc | Multifunctional chain shuttling agents |
JP2012067220A (en) * | 2010-09-24 | 2012-04-05 | Sekisui Chem Co Ltd | Insulating sheet and laminated structure |
FR2987838B1 (en) * | 2012-03-12 | 2014-04-11 | Univ Claude Bernard Lyon | TELECHELIC POLYOLEFIN AND PROCESS FOR OBTAINING THE SAME |
FR3029920B1 (en) | 2014-12-12 | 2016-12-09 | Univ Claude Bernard Lyon | FUNCTIONAL OR TELECHELIC POLYOLEFIN, ITS DERIVATIVES, AND PROCESS FOR PREPARING THE SAME |
-
2015
- 2015-12-08 FR FR1562012A patent/FR3044664B1/en not_active Expired - Fee Related
-
2016
- 2016-12-07 EP EP16809754.1A patent/EP3387024B1/en active Active
- 2016-12-07 CN CN201680072284.2A patent/CN108699171B/en active Active
- 2016-12-07 WO PCT/EP2016/080064 patent/WO2017097829A1/en active Application Filing
- 2016-12-07 JP JP2018530005A patent/JP6876700B2/en active Active
- 2016-12-07 US US15/781,366 patent/US10752713B2/en active Active
-
2018
- 2018-05-29 SA SA518391692A patent/SA518391692B1/en unknown
Also Published As
Publication number | Publication date |
---|---|
WO2017097829A1 (en) | 2017-06-15 |
FR3044664B1 (en) | 2017-12-29 |
JP6876700B2 (en) | 2021-05-26 |
FR3044664A1 (en) | 2017-06-09 |
CN108699171B (en) | 2021-09-03 |
US20180362681A1 (en) | 2018-12-20 |
EP3387024A1 (en) | 2018-10-17 |
JP2018536751A (en) | 2018-12-13 |
CN108699171A (en) | 2018-10-23 |
US10752713B2 (en) | 2020-08-25 |
SA518391692B1 (en) | 2022-08-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP3387028B1 (en) | Monofunctional or telechelic copolymer of 1,3-butadiene and ethylene | |
EP3230326B1 (en) | Functionalized or telechelic polyolefin, their derivatives and process to prepare tereof | |
EP3697826B1 (en) | Method for synthesising polymer blocks | |
EP3635052B1 (en) | Functional copolymer consisting of a 1,3-diene and an olefine | |
WO2018224774A1 (en) | Functional ethylene and 1,3-butadiene copolymer | |
EP3387024B1 (en) | Monofunctional or telechelic copolymer of 1,3-diene and ethylene or alpha-monoolefin | |
EP4251660A1 (en) | Catalyst system based on a rare-earth metallocene and a co-catalyst having a plurality of carbon-magnesium bonds | |
WO2018020124A1 (en) | Method for preparing a catalytic system comprising a rare-earth metallocene | |
EP4251659A1 (en) | Catalytic system based on a rare-earth metallocene and a co-catalyst having a plurality of carbon-magnesium bonds | |
EP4077419A1 (en) | Diorganomagnesium compound for catalytic system | |
EP4251668A1 (en) | Synthesis of block polymers based on 1,3-diene and ethylene | |
EP4251658A1 (en) | Co-catalyst comprising multiple magnesium carbon bonds | |
WO2022112693A1 (en) | Telechelic polymers based on ethylene and 1,3 diene | |
WO2023237380A1 (en) | Coupled polyethylenes or copolymers of ethylene and 1,3-diene, and process for the preparation thereof | |
WO2023237381A1 (en) | Process for the synthesis of polyethylenes or copolymers of ethylene and 1,3-diene having a terminal ketone function | |
EP4077418A1 (en) | Catalytic system based on a metallocene and a diorganomagnesium |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: UNKNOWN |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE |
|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
17P | Request for examination filed |
Effective date: 20180709 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
AX | Request for extension of the european patent |
Extension state: BA ME |
|
RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: D'AGOSTO, FRANCK Inventor name: THUILLIEZ, JULIEN Inventor name: MACQUERON, BENOIT Inventor name: NORSIC, SEBASTIEN Inventor name: BOISSON, CHRISTOPHE |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: COMPAGNIE GENERALE DES ETABLISSEMENTS MICHELIN |
|
DAV | Request for validation of the european patent (deleted) | ||
DAX | Request for extension of the european patent (deleted) | ||
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: EXAMINATION IS IN PROGRESS |
|
17Q | First examination report despatched |
Effective date: 20210419 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: EXAMINATION IS IN PROGRESS |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
INTG | Intention to grant announced |
Effective date: 20220902 |
|
GRAJ | Information related to disapproval of communication of intention to grant by the applicant or resumption of examination proceedings by the epo deleted |
Free format text: ORIGINAL CODE: EPIDOSDIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: EXAMINATION IS IN PROGRESS |
|
INTC | Intention to grant announced (deleted) | ||
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
INTG | Intention to grant announced |
Effective date: 20230302 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE PATENT HAS BEEN GRANTED |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D Free format text: NOT ENGLISH |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602016081409 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D Free format text: LANGUAGE OF EP DOCUMENT: FRENCH |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG9D |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20230726 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MK05 Ref document number: 1591874 Country of ref document: AT Kind code of ref document: T Effective date: 20230726 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20231027 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20231126 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: RS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20231127 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20231026 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20231126 Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20231027 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20231222 Year of fee payment: 8 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602016081409 Country of ref document: DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SM Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R119 Ref document number: 602016081409 Country of ref document: DE |
|
26N | No opposition filed |
Effective date: 20240429 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20231207 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20231207 |
|
REG | Reference to a national code |
Ref country code: BE Ref legal event code: MM Effective date: 20231231 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20230726 Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20231207 |